TWI294913B - Liquid containing diatom and method for culturing diatom - Google Patents
Liquid containing diatom and method for culturing diatom Download PDFInfo
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- TWI294913B TWI294913B TW092133576A TW92133576A TWI294913B TW I294913 B TWI294913 B TW I294913B TW 092133576 A TW092133576 A TW 092133576A TW 92133576 A TW92133576 A TW 92133576A TW I294913 B TWI294913 B TW I294913B
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- C12N1/00—Microorganisms, 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
- C12N1/12—Unicellular algae; Culture media therefor
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- A01—AGRICULTURE; FORESTRY; ANIMAL HUSBANDRY; HUNTING; TRAPPING; FISHING
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Description
1294913 玖、發明說明: 【發明所屬之技術領域】 本發明係關於使用料填、珠母等貝類,大蝦、草蝦等 甲殼類,海參、海膽等棘皮類等水產種苗之飼養之微細藻 類之秒,藻,詳述之則係W於含該碎藻之液體及碎藻之培養 方法。 ^ 【先前技術】 貝類、甲殼類及棘皮類等水產種苗之養殖用飼料中,最 近被分類為角毛藻屬(Chaetoceros)及三角褐指藻屬 (Phaeodactylum)等之微細藻類之矽藻(如角毛藻屬之鈣質角 毛漢(ca/c/ir⑽s)、牟氏角毛藻(gMd/b)等)備受注目。 例如,鈣質角毛藻(C.⑶化办⑽幻由於在其4根角均有^条 長鞭毛,而由於該角毛藻之直徑(長度)祇有約3〜6 ,頗 適合水產種苗幼生時期之飼料。 微細藻類之一種、矽藻所含微量礦物質及維生素,均優 於其他植物浮游生物且均衡。此外,矽藻具有ΕρΑ(廿碳五 烯類:一種多價不飽和脂酸)及DHA(廿二碳六缔酸;一種 多價不飽和脂酸)等有用脂酸。由於上述理由,微細藻類, 矽藻乃係一種評價非常高之飼料。 然而,穩定培養微細藻類之工作卻非常困難。如「丨争 類繁殖技術試驗、(1)鹹水種苗生產研究、生物飼料之培 (以下稱為文獻1)及「平成4年(1992)度特定研究開發促進 事業微小藻類之大量培養技術開發研究報告書」(以τ $ 為文獻2)報告指出,依據先前培養方法製得之_質角毛、菜 1294913 (C,似)(以下簡稱角毛藻)之細胞濃度之上限為約 3·〇χ 1 013細胞/m3。該細胞濃度係指培養液每1 m3之細胞數而 言。 由於依據先前之培養方法,角毛藻之細胞濃度之上限為 約3·〇χ10π細胞/m3 ’其培養量並未達十分理想,於是極需 一種能穩定且高濃度培養角毛藻之液體(培養基,培養液) 及培養方法。 【發明内容】 本發明係鑑於上述情勢而達成者,其目的為提供一種能 將微細藻類之一種,矽藻以高濃度且穩定培養之含矽藻液 體及秒蕩培養方法且提供藉由上述方法培養之碎、藻。 為達成上述目的,本發明提供一種培養矽藻用之液體, 其特徵為含有>5夕藻、碎及氮,且將上述珍與上述氮之質量 ;辰度比石夕/氮設定為〇 · 18以上之含硬藻液體。 為達成上述目的,本發明提供一種碎藻,其特徵為在含 有石夕及氮,且將上述矽與上述氮之質量濃度比矽/氮設定於 〇 · 18以上之液體中培養。 依據本發明,為培養矽藻用之液體所含之矽與氮之質量 濃度比之矽/氮係設定於0.18以上,因此得以高濃度且穩定 培養矽藻。 為達成上述目的,本發明提供一種培養矽藻用之液體, 其特欲為含有秒藻、磷、矽及氮,且將上述磷與上述氮之 質量濃度比磷/氮,及上述矽與上述氮之質量濃度比、矽/ 氮係分別設定於〇 · 1以上之含矽藻液體。 1294913 為達成上述目的,本發明提供一種矽藻,其特徵為該矽 藻係在含有磷、氮及矽,且將上述磷與上述氮之質量濃度 比% /氮,及上述矽與上述氮之質量濃度比矽/氮分別設定為 〇 _ 1以上之液體中培養。 依據本發明,培養矽藻用之液體所含之磷與氮之質量濃 度比磷/氮及矽與氮之質量濃度比之矽/氮係分別設定於〇1 以上’因此得以局濃度且穩定培養石夕薄。 為達成上述目的,本發明提供一種含矽藻液體,其特徵 為培養矽藻用之液體,且含有矽藻、磷、矽及氮,而其pH 值係在6.4以上而8.4以下。 為達成上述目的,本發明提供一種矽藻,其特徵為在含 有¥、氮及矽,且將其pH值設定於64以上8·4以下之範圍 之液體中培養。 依據本發明,培養矽藻用之液體之pH係設定於6·4以上 8.4以下之範圍,因此得以高濃度且穩定培養矽藻。 為達成上述目的,本發明提供一種矽藻培養方法,其特 徵為以含有氮及矽之矽藻培養用液體培養矽藻之方法,且 孩培養方法係由預先測定上述液體所含氮之初期濃度及矽 义初期濃度之事前測定步.驟,將上述矽藻接種於上述液體 之接種步騾,分別測足上述氮之補給前濃度及上述矽之補 給則濃度之補給前測定步騾,為計算上述氮之初期濃度與 =給前濃度之氮濃度差距,及上述矽之初期濃度與補給前 /辰度之矽濃度差而實施之濃度差測定步騾,以及根據上述 氮濃度差及上述矽濃度差距,分別決定對上述液體補給之 1294913 氮量及矽量,以使上述氮之初期濃度與上述矽之初期濃度 比率一致而補給於上述液體之補給步騾所構成。 依據本發明,於接種矽藻之前測定氮之初期濃度及矽之 初期濃度,而於補給氮及矽之前測定氮之補給前濃度及矽 之補給前濃度。然後根據氮之初期濃度與補給前濃度之氮 濃度差距,及矽之初期濃度與補給前濃度之矽濃度差距, 決定補給於液體之氮量及矽量。於是得以保持氮之質量濃 度與矽之質量濃度之比率於一定,因此得以高濃度且穩定 培養珍藻。 為達成上述目的,本發明提供一種矽藻培養方法,其係 使用含氮及石夕之石夕藻培養用液體,培養秒藻之方法,其特 徵為該方法係由分別測定上述氮之補給前濃度及上述矽之 補給前濃度之補給前測定步騾,分別計算上述氮之規定濃 度與補給前濃度之氮濃度差距,及上述矽之規定濃度與補 給前濃度之矽濃度差距之濃度測定步騾,以及根據上述氮 濃度差及矽濃度差,分別決定補給於上述液體之氮量及矽 量以使上述氮之規定濃度及上述矽之規定濃度之比率一致 而補給於上述液體之補給步驟所構成。 依據本發明,於補給氮及矽之前測定氮之補給前濃度及 矽之補給前濃度後,根據氮之規定濃度與補給前濃度之氮 濃度差及矽之規定濃度與補給前濃度之矽濃度差決定補給 於液體之氮量及矽量,因此氮之質量濃度與矽之質量濃度 之比率係經常保持於一定,得以高濃度且穩定培養石夕蕩。 為達成上述目的,本發明提供一種矽藻培養方法,其係 1294913 使用含氮及秒之#培養用液體培養沙藻之培養方法,其 特徵為由分別測定接種上述,夕藻之液體所含氮之初期濃度 切之初期濃度之事前測定步驟,分別測定上述氮之補給 則濃度及上述梦之補給前濃度之補給前敎步驟,分別計 弃上述氮之初期濃度與補給前濃度之氮濃度差及上述石夕之 初期濃度與補給前濃度切濃度差之濃度差測定步驟,及 根據上述氮濃度差及上述秒濃度差,分別決定補給於上述 現體之氮量及秒量’以使其比率與上述氮之初期濃度與上 切之初職度之時-致,而將其補給於上述液體之補 給步驟所構成。 依據本發明,於接㈣藻錢即測定氮之初期濃度及珍 <初期濃度,而於補給氮及以前測定氮之補給前濃度及 石夕^補給前濃度。’然後,根據氮之初期濃度與補給前濃度 瘦度差及秒之初期濃度與補給前濃度之矽濃度差,決 2給於液體之氮量切量。因此,氮之質量濃度㈣之 只里瑕度《比率係經常保持定’得以高濃度且穩定培 養石夕讓。 為達成上述目的,本發明提供一種矽藻培養方法,其係 使用含有氮及矽之培養用液體培養矽藻之方法,其特徵為 $於接種上述碎藻之耗用量測定用液體分別測定由上述珍 ,耗用之氮耗用量及料用量之事前測定步驟,將上述珍 藻接種於培養用液體之接種步驟,測定上述矽藻之細胞濃 2測定步驟’當上述細胞濃度超過規定量時調配追肥用液 體以使氮/矽比率略與上述氮耗用量與上述矽耗用量比率 1294913 -致之調整步職將上心 體之補給步驟所構成。 用,夜胆補給於上述培養用液 依據本發明,於耗用量 用之氮耗用量及$耗用量 心’分別計測㈣蕩耗 當碎藻之細胞濃度超過規於Μ用㈣培切藻時, 氮耗用量與料用量之其氮率則調整為略與 質量濃度係經常保持於—定=°因此’氮質量濃度與石夕 矽藻。 、 由此得以高濃度且穩定培養1294913 玖, the invention description: [Technical Field] The present invention relates to the use of material filling, pearls and other shellfish, prawns, grass shrimp and other crustaceans In the second, the algae, in detail, is a method of cultivating the liquid and the algae containing the algae. ^ [Prior Art] Among the feeds for aquaculture seedlings such as shellfish, crustaceans, and echinoderms, they have recently been classified as the algae of the microalgae such as Chaetoceros and Phaeodactylum. Calcareous horny horns (ca/c/ir(10)s), Chaetoceros gracilis (gMd/b), etc. are highly attractive. For example, C. oxysporum (C. (3) Chemicals (10) illusion has a long flagella in its four corners, and because the diameter (length) of the horned algae is only about 3 to 6, it is quite suitable for the aquatic seedlings. The feed. The microalgae, the trace minerals and vitamins contained in the algae, are superior to other plant plankton and are balanced. In addition, the algae have ΕρΑ (廿 pentadecene: a polyvalent unsaturated fatty acid) and Useful fatty acids such as DHA (dihexamethylenedicarboxylic acid; a polyvalent unsaturated fatty acid). For the above reasons, microalgae, algae are a highly evaluated feed. However, the work of stably cultivating microalgae is very Difficulties. For example, "Study on the breeding technology of the competition, (1) research on the production of salt water seedlings, cultivation of biological feeds (hereinafter referred to as the literature 1), and large-scale cultivation techniques of microalgae in the specific research and development promotion of the Heisei 4 years (1992). According to the report of the Development Research Report (with τ $ for the literature 2), the upper limit of the cell concentration of the genus horned horn and the vegetable 1294913 (C, like cerevisiae) based on the previous culture method is about 3 ·〇χ 1 0 13 cells/m3. The cell concentration refers to the number of cells per 1 m3 of the culture solution. Since the upper limit of the cell concentration of C. cerevisiae is about 3·〇χ10π cells/m3' according to the previous culture method, It is not ideal, so there is a great need for a liquid (culture medium, culture solution) and culture method for cultivating Chaetoceros in a stable and high concentration. SUMMARY OF THE INVENTION The present invention has been made in view of the above circumstances, and its object is to provide an energy source. A kind of microalgae, a high concentration and stable culture of the algae-containing liquid and a second culture method, and providing the crushed algae cultured by the above method. To achieve the above object, the present invention provides a cultured algae. a liquid containing a hard algae liquid containing > 5 algae, minced and nitrogen, and having the above-mentioned qualities of the above-mentioned nitrogen and the ratio of the nitrogen to the cerium/nitrogen of 〇·18 or more. The present invention provides a pulverized algae, which is characterized in that it contains zephyr and nitrogen, and the sputum is cultured in a liquid having a mass concentration ratio of 氮/nitrogen of 氮·18 or more. The ratio of the mass concentration of cerium to nitrogen contained in the liquid for the algae is set at 0.18 or more, so that the algae can be cultured at a high concentration and stably. To achieve the above object, the present invention provides a liquid for cultivating algae. Specifically, it is characterized in that it contains second algae, phosphorus, antimony and nitrogen, and the mass concentration ratio of the phosphorus to the nitrogen is phosphorus/nitrogen, and the mass concentration ratio of the niobium to the nitrogen and the niobium/nitrogen system are respectively set to 〇· 1 or more of the algae-containing liquid. 1294913 In order to achieve the above object, the present invention provides an algae, characterized in that the algae are contained in phosphorus, nitrogen and strontium, and the mass concentration ratio of the phosphorus to the nitrogen is % / nitrogen. And the above-mentioned cesium is cultured in a liquid having a mass concentration ratio 矽/nitrogen of 〇_1 or more, respectively. According to the present invention, the concentration of phosphorus and nitrogen contained in the liquid for cultivating diatoms is higher than that of phosphorus/nitrogen and The ratio of the mass concentration of cerium to nitrogen is set to 〇1 or more, respectively, so that the local concentration is stabilized and the culture is thin. In order to achieve the above object, the present invention provides a liquid containing diatoms which is characterized by cultivating a liquid for diatoms and containing diatoms, phosphorus, strontium and nitrogen, and having a pH of 6.4 or more and 8.4 or less. In order to achieve the above object, the present invention provides a diatom bacterium which is cultured in a liquid containing ¥, nitrogen and hydrazine and having a pH of 64 or more and 8.4 or less. According to the present invention, the pH of the liquid for cultivating the algae is set to be in the range of 6.4 or more and 8.4 or less, so that the algae can be cultured at a high concentration and stably. In order to achieve the above object, the present invention provides a method for cultivating a diatom bacterium, which is characterized in that a method for cultivating diatoms in a liquid for cultivating algae containing nitrogen and strontium is used, and the method for cultivating the larvae is to preliminarily determine the initial concentration of nitrogen contained in the liquid. And the pre-measurement step of the initial concentration of the initial sense, the above-mentioned diatoms are inoculated into the inoculation step of the liquid, and the measurement of the concentration of the nitrogen before the replenishment of the nitrogen and the concentration of the recharge of the sputum are measured, and the calculation is performed. a concentration difference measurement step performed by the difference between the initial concentration of nitrogen and the concentration of nitrogen before the concentration, and the concentration difference between the initial concentration of the enthalpy and the enthalpy before and after the replenishment, and the difference between the nitrogen concentration and the enthalpy concentration The difference is determined by the amount of nitrogen and the amount of nitrogen supplied to the liquid 1294913, respectively, so that the initial concentration of the nitrogen is equal to the initial concentration ratio of the above-mentioned enthalpy, and the supply step of the liquid is replenished. According to the present invention, the initial concentration of nitrogen and the initial concentration of strontium are measured before inoculation of diatoms, and the pre-recharge concentration of nitrogen and the pre-recharge concentration of hydrazine are measured before nitrogen and strontium supplementation. Then, based on the difference between the initial concentration of nitrogen and the concentration of nitrogen before recharge, and the difference between the initial concentration of strontium and the concentration before recharge, the amount of nitrogen supplied to the liquid and the amount of strontium are determined. Therefore, it is possible to maintain a constant ratio of the mass concentration of nitrogen to the mass concentration of strontium, thereby enabling high concentration and stable cultivation of rare algae. In order to achieve the above object, the present invention provides a method for cultivating a diatom algae, which is a method for culturing a second algae using a liquid containing nitrogen and a liquid for cultivation of Shigata sinensis, characterized in that the method is performed by separately measuring the supply of nitrogen before the replenishment. The concentration and the pre-recharge concentration of the above-mentioned hydrazine are measured before the replenishment, and the difference between the nitrogen concentration of the predetermined concentration and the pre-recharge concentration, and the concentration difference between the sputum concentration of the sputum and the pre-supplement concentration are respectively determined. And determining, according to the difference in nitrogen concentration and the concentration of ruthenium, the amount of nitrogen supplied to the liquid and the amount of ruthenium, respectively, such that the ratio of the predetermined concentration of the nitrogen and the predetermined concentration of the enthalpy are equalized to supply the liquid to the replenishing step. . According to the present invention, before the nitrogen supply and the strontium are measured, the pre-recharge concentration of nitrogen and the pre-recharge concentration of strontium are determined, and the difference between the nitrogen concentration of the predetermined concentration and the pre-recharge concentration and the enthalpy concentration difference between the sputum concentration and the pre-supplement concentration are determined. The amount of nitrogen and the amount of helium to be supplied to the liquid are determined. Therefore, the ratio of the mass concentration of nitrogen to the mass concentration of strontium is often maintained at a constant level, so that a high concentration and stable culture can be achieved. In order to achieve the above object, the present invention provides a method for cultivating diatoms, which is a method for cultivating sand algae using a nitrogen-containing and second-time culture liquid, which is characterized by separately measuring nitrogen contained in the liquid of the above-mentioned Japanese algae. The pre-measurement step of the initial concentration of the initial concentration cut, and the pre-replenishment step of the concentration of the nitrogen supply and the pre-recharge concentration of the dream are respectively measured, and the difference between the initial concentration of the nitrogen and the concentration of the nitrogen before the recharge is discarded. a concentration difference measuring step of the difference between the initial concentration of the stone stalk and the concentration before the replenishment concentration, and determining the amount of nitrogen and the amount of second supplied to the present body based on the difference in the concentration of nitrogen and the difference in the second concentration to make the ratio When the initial concentration of nitrogen and the initial degree of the upper cut are the same, it is supplied to the replenishing step of the liquid. According to the present invention, the initial concentration of nitrogen and the initial concentration of the nitrogen are measured in the (4) algae money, and the nitrogen concentration and the pre-recharge concentration before the recharge and the pre-recharge concentration before the recharge are measured. Then, based on the difference between the initial concentration of nitrogen and the pre-recharge concentration, the difference between the initial concentration of the second and the concentration before the recharge, the amount of nitrogen applied to the liquid is determined. Therefore, the concentration of nitrogen (4) is only a constant degree, and the ratio is often kept constant to achieve high concentration and stable cultivation. In order to achieve the above object, the present invention provides a method for cultivating diatoms, which is a method for cultivating diatoms using a culture liquid containing nitrogen and strontium, which is characterized in that: The pre-measurement step of the above-mentioned rare nitrogen consumption and the amount of the raw material, the inoculation step of inoculating the rare algae in the culture liquid, and measuring the cell concentration of the above-mentioned algae 2 determination step 'when the concentration of the above cells exceeds a prescribed amount The topdressing liquid is prepared by blending the liquid for top dressing so that the nitrogen/rhenium ratio is slightly different from the above-mentioned nitrogen consumption amount and the above-mentioned consumption ratio 1294913. For the above-mentioned culture liquid for use in the above-mentioned culture liquid, according to the present invention, the nitrogen consumption and the consumption amount of the consumption amount are respectively measured (4), and the cell concentration of the algae is more than the standard (4) In the case of algae, the nitrogen consumption and the nitrogen content of the feed amount are adjusted to be slightly different from the mass concentration system, which is often maintained at -== thus the 'nitrogen mass concentration and the algae. , thereby achieving high concentration and stable culture
【實施方式】 本實施形態,首先實施5種實 I釦及刀析作為事前調查,探 測為穩定而高濃度培養矽蔆浼 晉吵條件。然後,根據該條件探 討為穩定而高濃度培養矽藻之方法。 (事前調查) 首先記述接種於液體(培養液)中之角毛藻培養量之變化 (繁殖量)與構成該培養液之成分之耗用量之關係。 準備具有如圖1之培養成分,且成分組成比係互相不同之 11種試料。將各試料放進一定容量(例如約65xl(r3m3)之戶 _ 外用(天然光用)密閉型反應器。各試料中之培養液容量均一 定。然後將規定細胞數之角毛藻接種於各反應器。經過— 定時間後測定每一試料之細胞濃度之變化[(培養細胞濃 度Μ初期細胞濃度)];單位··細胞/m3)、氮耗用量、磷耗用 量及矽耗用量。氮(N),磷(P)及矽(Si)係培養角毛藻時之重 要成分元素。 圖1所示之SEALIFE(MARINETECH公司製),溶解於水則 -11 - 1294913 乂海水。祇要溶解於水則 《成分。" 4水,SEAUFE以外 或藥品滅菌:二’不可使用經高壓減菌、過濾滅菌 氮耗用!:海水或未殺菌之天然海水。 濃度[(初二養::培養硬之容量—定,可用耗用之質量 毛用I亦由於各培養液之容 — 濃度[(初期培養液中之磷質量濃产二:用耗用之質量 示石:蹲質量濃度之單位為(二;:留磷質量濃度”表 濃於各培mm,可用耗用之質量 示。、請養液中切質量濃度)(殘留鱗質量濃度)]表 圖2表示π種試料之各培養液之細胞 /m3)’氮耗用量,磷耗用量及魏用量。& f化(細胞 、根據該測定結果晝出之氮耗用量與角毛藻細胞濃度變化 :關係’瑪耗用量與角毛藻細胞濃度變化之關係切耗用 3量c與角毛藻細胞濃度變化之關係’分別如圖3A、圖3B及圖 如圖3A、圖3B及圖3C之二點虛線所示,氮、磷及矽之各 耗用量與細胞變化量(繁殖量)之間有正比關係。 第一步驟係記錄培養液成分中磷與氮之質量濃度比之 P/N值及矽與氮之質量濃度比之Si/N值。 揭示先前培養方法之文獻1及2均記載角毛藻培養液中之 氮、磷及矽之各質量濃度。文獻1所記載之培養液中之氮質 -12- 1294913 量濃度’磷質量濃度及矽質量濃度,分別為13.8(ppm),1.4 (ppm)’ 0.15(ppm)。文獻2所記載之培養液中之氮質量濃度, 磷貝里;辰度’秒質量濃度’分別為1 〇2(ppm),1 ·4 (ppm), 8.0(ppm)。 文獻1之培養液中之p/N,Si/N分別為0.10及0.011,而文 獻2之培養液中之?以,8丨/1^則分別為0.014及0.078。 如圖3A,3B及3C所示,氮,磷及矽之各耗用量與細胞濃 度變化量之間有比例關係,既然P/N及Si/N係根據文獻1及 文獻2計算,祇要使用該比率設定於0· 1以上之培養液,其 角毛藻繁殖量應較先前培養方法為大。 此外,如圖3A,3B及3C中之虛線所示,倘要提昇角毛藻 之細胞濃度至約6_〇χ1013細胞/m3以上,似乎宜使用將氮質 量濃度調整為約160 ppm以上,而將磷質量濃度調整為約20 PPm以上及將矽質濃度調整為約60 ppm以上之培養液。 於是,為查證上述二項推論,調配具有圖4之成分組成之 培養液1〜培養液6。至於培養液7之成分組成係文獻1所記載 之培養液之成分組成,而培養液8之成分組成係文獻2所記 載之培養液之成分組成。各培養液中之氮質量濃度,磷質 量濃度,矽質量濃度,P/N及Si/N則分別表示於圖5。 培養液1之磷質量濃度及矽質量濃度係小於上述推論 值。培養液1中之氮質量濃度,磷質量濃度,矽質量濃度係 分別為 166(ppm),l〇(ppm),30(ppm),而 p/N,Si/N則分別 為 0.06及 0.18。 培養液2之磷質量濃度係調整為培養液1之2倍(磷質量濃 1294913 度=20(ppm),p/n=〇12)。 培養液3之矽質量濃度係調整為培養液1之2倍(矽質量濃 度=60(ppm),si/N=0.36)。 培養液4之磷質量濃度及矽質量濃度係分別調製為培養 液1之2倍(磷質量濃度=20(ppm),Ρ/Ν=0·12,矽質量濃度=60 (ppm),Si/N=〇.36)。 培養液5之矽質量濃度係調整為培養液2之3倍(矽質量濃 度=90(ppm),si/N=0.54)。 培養液6之矽質量濃度係調整為培養液2之4倍(矽質量濃 度= 120(ppm),si/N=0.72)。 培養液2-6之磷質量濃度,矽質量濃度,p/N& Si/N,相 車父於先前組成成分之培養液7及8之磷質量濃度,夕質量濃 度,P/N,Si/N均高。 第三步驟係具有較高磷質量濃度及矽質量濃度之培養液 中之pH值與水解量之關係。 針對培養液成分之一之碳酸氫鈉(NaHc〇3)之質量濃度加 以凋1,使培養液4之pH在7.0〜9.0之間變化。同時測定於培 養液4產生之水解量(測定溶液每im3產生之水解物質量 (kg))。期間對培養液4供給混合為維持培養液内生命而必須 之成分、3°/。碳酸氣之空氣,作為培養液4通氣攪拌用。 孩測疋結果如圖6。圖6之實線及虛線分別表示於不同實 驗日所得水解量變化,兩者結果略一致。 由於測定獲悉,當培養液4之pH超過8·5後,水解量變化 則加速,水解量(沉澱量)增加。而培養液々之口^超過8乃以 1294913 後:,澱物中則含有角毛藻,角毛藻不再繁殖。 弟四步驟係測定培養液之阳值上限。該實驗係使用培養 =成^之-之碳酸氫鈉及混合3%碳酸氣之空氣調整pH—, =而σ &酸氫納量增加,溶液之pH值亦昇冑,而碳酸氣 辰度^加’洛液心pH值則減少。碳酸氯納及碳酸氣係供給 角毛藻進行光合作用時之碳源’同時扮演培養液之pH調整 劑角色。 將培養液1(11 〇x l〇-3m3)放進設置於戶外之密閉型反應 器:維持溫度於約25°C之下,將光量子量約12〇0_ol/mVs · 強度〈自&太陽光照射於培養液上。在該狀態下實施2項測 疋第一項係以混合3%碳酸氣之空氣通氣攪拌培養液i, 4疋培養液1中之角毛藻細胞濃度之經時變化及之時間 又化。第二項係添加碳酸氫鈉(7 0xl03 後再用空氣通 氣才見拌培養液1 別測定培養液i中之角毛藻細胞濃度之 時間變化及pH之時間變化。 測疋結果如圖8。圖8之實線係第一項測定之結果,亦即 表不不添加碳酸氫鈉之下以混合3%碳酸氣之空氣通氣攪· 拌時之培養液1之pH之時間變化。圖8之虛線係第二項測定 、^果亦即表示添加碳酸氫鈉之下,祇以空氣通氣撥拌 時之培養液1之pH之時間變化。 由上述測走結果獲悉,對培養液丨以空氣通氣攪拌,且添 加碳酸氫納時,當培養液kpH超過8.5則產生沉殿。此時, 角毛藻則與沉澱物共沉。而以混合3%碳酸氣之空氣通氣攪 拌且不添加碳酸氫鈉時,培養液1之pH則逐漸降低。 -15- 1294913 由第三及第四項測定妹 ^ ^ 。 又心’對培養液添加碳酸氫鈉 時’右*以混合3%竣酸翕夕办与、s a 、 、 二亂通軋攪拌培養液則可將pH設 疋於8.4以下。結果得防止沉澱產生及角毛藻之共沉。 - 至於培養液1之成分,相較於培養液2〜6之成分,除P/N ; 或Si/N以外,其他成分則相同。因此,培養以之溶解度與 其他培養液之溶解度格同,使用其他培養液時,若於對培 養液添加碳酸氫勒之狀態下’以混合碳酸氣之空氣通氣攪 掉培養液,則應可防止沉殿之產生及角毛薄之共沉現象。 第五步驟係關於培養液之p H下限值及碳酸氫鈉之適宜添· 加量範圍。 改’交培養液成分之一之碳酸氫鈉之質量濃度,調整下列8 種培養液1,以混合3%碳酸氣之空氣,通氣攪拌培養液J。 [l]0.02xl03 ppm^ [2]0.07xl〇3 ppm , [3]〇.14xl〇3 ppm , [4]〇.28 xlO3 ppm,[5]0·56χ103 ppm,[6]1.OxlO3 ppm,[7]2〇χ1〇3 ppm,[8]7·〇χ 1〇3 ppm。對如上調製之各培養液ι,實施角毛 藻培養實驗,測定細胞濃度之時間變化及pH之時間變化。 · 為確保再現性,上述實驗係於不同日實施4次。 圖9及1 0係第一次測定結果。第1次培養實驗係使用具有 下列3種碳酸氫鈉質量濃度之培養液1 : [ι]〇·〇2χΐ〇3 ppm, [3]0.14xl03 ppm,[6]l.〇xl03 ppm。圖 9所示 XI,X2及 X3係 分別表示以[1]0·02χ103 ppm,[3]0·14χ103 ppm,[6]1·〇χ103 ppm之培養液培養之角毛藻之細胞濃度之時間變化。圖ι 〇 所示 ΧΑ 卜 ΧΑ2及 ΧΑ3 則分別表示[1]〇·〇2χ103 ppm,[3]〇·14χ 1 〇3 ppm,[6] 1 ·〇χ 103 ppm之培養液1之pH之時間變化。 -16 - 1294913 圖11及12係第二次測定結果。第二次培養實驗係使用具 有下列4種碳酸氫鈉質量濃度之培養液1 : [2]〇 〇7xl〇3 ppm, [3]0·14χ103 ppm,[4]0·28χ103 ppm 及[6]1·〇χ1〇3 ppm。圖 u 之 Y卜 Y2,Y3,Y4 分別表示以[2]〇.〇7xi〇3 ppm,[3]〇.ΐ4 χΙΟ3 ppm,[4]0.28xl03 ppm 及[6]1·〇χ1〇3 ppm之培養液以養之角 毛藻細胞濃度之時間變化。而圖12之ya卜YA2,YA3、YA4 則分別表示[2]0.07><10 ppm ’ [3]0·14χ103 ppm,[4]0·28 xlO3 ppm及[6]l.〇xl03 ppm之培養液1之pH之時間變化。 圖13及圖14係第三次測定結果。第三次培養試驗係使用4 種具有下列碳酸氫氣質量濃度之培養液1 : [4]〇.28χ103 ppm,[5]0.56xl03 ppm,[6]l.〇xl〇3 ppm及[7]2·〇χ1〇3 ppm。 圖 13所示 Z1,Z2, Z3,Z4分別表示以[4]〇·28χ103 ppm,[5]0·56 xlO3 ppm,[6]l.〇xl03 ppm 及[7]2.〇xl〇3 ppm 之培養液 1 培養 之角毛藻細胞濃度之時間變化。而圖14之ZA1,ZA2,ZA3, ZA4 則分別表示[4]0·28χ103 ppm,[5]0.56x 103 ppm,[6]1·0 xlO3 ppm及[7]2.0 xlO3 ppm之培養液1之pH之時間變化。 圖15及16係第四次測定結果。第四次培養實驗係使用含 有下列2種碳酸氫鈉質量濃度之培養液1 : [6] 1.0x1 〇3 ppm, [8]7·〇χ103 ppm。圖 15 之 Wl,W2 分別表示以[6]1·〇χ1〇3 ppm,[8]7.〇xl〇3 ppm之培養液1培養之角毛藻細胞濃度之時 間變化。而圖16之WA1,WA2則分別表示[6]l_〇xl〇3 ppm, [8]7·0 xlO3 ppm培養液1之pH之時間變化。 由上述測定結果獲知下列結果。 [1]在0.02X 103 ppm之培養液1,pH值係於開始實驗後立即 1294913 下降’於約25小時後降到6.4以下,且細胞濃度則未達3 細胞/m3。 [2] 在0.07X1G3 ppm之培養液1,其pH值係維持於約以 上而約7.0以下《範圍,而細胞濃度則達3χ1〇η細胞~3。 [3] 在〇.14xH)3 ppm之培養^,其pH值係維持於約u以 上而約7.4以下範園,而細胞濃度則超過4χ1〇π細胞^3。 [4] 在0.28X1G3 ppm之培養液!,其_直係維持於約"以 上而約7.6以下之範圍,而其細胞濃度則達4χΐ〇13細胞以 上。 [5] 在0.56Χ103 ppm之培養液1,其ρΗ值係維持於約Μ以 上而約7.6以下範圍,而其細胞濃度則達4><1〇13細胞/^以 上。 [6] 在l.〇xl〇3ppmi培養液1,其?1^值係維持於約6·4以上 而約7.9以下範圍,而其細胞濃度則達6χ1〇13細胞/瓜3以上。 [7] 在2.0xl03ppm之培養液丄,其pH值係維持於約7〇以上 而約8.1以下範圍,而細胞濃度則達5χ1〇13細胞/m3以上。 [8] 在7.0xl03ppm之培養液!,其pH值係維持於約6·7以上 而約8.1以下範圍,而細胞濃度則達3χ1〇13細胞/m3以上。 因此,調製一種碳酸氫鈉質量濃度高於〇〇2xl〇3ppm以上 之培養液1後,以混合3%碳酸氣之空氣通氣攪拌,並將培 養液1之pH設定於6.4以上,且可使角毛藻之細胞濃度超過 先前之培養方法所達到之角毛藻細胞濃度之上限值(3χΐ〇π 細胞/m3)。[Embodiment] In the present embodiment, first, five kinds of real buckles and knife analysis were carried out as a preliminary investigation, and it was found that the conditions of stable and high concentration culture of 矽菱浼 were raised. Then, a method of cultivating the algae at a high concentration in a stable manner was examined based on the conditions. (Pre-investigation) First, the relationship between the change in the amount of cultured Chaetoceros inoculated in the liquid (culture medium) (the amount of reproduction) and the consumption of the components constituting the culture solution will be described. Eleven samples having the culture components as shown in Fig. 1 and having different composition ratios were prepared. Each sample is placed in a fixed capacity (for example, about 65 x 1 (r3 m3) of households - external (natural light) closed type reactor. The volume of the culture solution in each sample is constant. Then, the specified number of cells is inoculated into each Reactor. After a certain period of time, determine the change in cell concentration of each sample [(culture cell concentration Μ initial cell concentration)]; unit · · cells / m3), nitrogen consumption, phosphorus consumption and consumption the amount. Nitrogen (N), phosphorus (P) and strontium (Si) are important constituent elements for the cultivation of Chaetoceros. SEALIFE (manufactured by MARINETECH Co., Ltd.) shown in Fig. 1 is dissolved in water and -11 - 1294913. As long as it dissolves in water, the ingredients. " 4 water, other than SEAUER or drug sterilization: two 'can not be used by high pressure reduction, filtration sterilization nitrogen consumption!: seawater or unsterilized natural seawater. Concentration [(the first two raises:: the capacity of the culture hard - set, the quality of the available hair is also used because of the capacity of each culture solution - concentration [(the initial quality of phosphorus in the culture solution is concentrated 2: the quality of consumption) Shishi: The unit of mass concentration of 蹲 is (2;: the concentration of phosphorus remaining) is thicker than each meter mm, and can be used for the quality of the consumption. Please check the mass concentration of the nutrient solution) (residual scale mass concentration)] 2 indicates the cells of each culture solution of π kinds of samples/m3) 'nitrogen consumption amount, phosphorus consumption amount and Wei dosage. & f (cell, nitrogen consumption according to the measurement result and Chaetoceros Changes in cell concentration: relationship between the amount of consumption and the change of cell concentration of Chaetoceros chinensis. The relationship between the amount of c and the change of cell concentration of Chaetoceros sinensis is shown in Figure 3A, Figure 3B and Figure 3A, Figure 3B, respectively. And the dotted line of Fig. 3C shows that there is a proportional relationship between the consumption of nitrogen, phosphorus and strontium and the amount of change in cell growth (the amount of reproduction). The first step is to record the mass concentration ratio of phosphorus to nitrogen in the composition of the culture solution. The P/N value and the mass concentration ratio of cerium to nitrogen are Si/N values. The literatures 1 and 2 revealing the previous culture methods all describe the angle. The concentration of nitrogen, phosphorus and strontium in the algae culture solution. The concentration of nitrogen in the culture solution described in the literature 1 - 1294913 concentration and the mass concentration of strontium are 13.8 (ppm), 1.4 ( Ppm)' 0.15 (ppm). The mass concentration of nitrogen in the culture solution described in the literature 2, phosphorus berry; the end of the 'secondary mass concentration' are 1 4 2 (ppm), 1 · 4 (ppm), 8.0 ( Pp/N, Si/N in the culture solution of Document 1 is 0.10 and 0.011, respectively, and in the culture solution of Document 2, 8丨/1^ are respectively 0.014 and 0.078. As shown in Fig. 3A, As shown in 3B and 3C, there is a proportional relationship between the amount of nitrogen, phosphorus and strontium and the amount of change in cell concentration. Since P/N and Si/N are calculated according to literature 1 and literature 2, as long as the ratio is used, For culture medium above 0·1, the amount of cultured Chaetoceros should be larger than that of the previous culture method. In addition, as shown by the dotted lines in Figures 3A, 3B and 3C, if the cell concentration of Chaetoceros sp. is raised to about 6_〇 Χ1013 cells/m3 or more, it seems appropriate to adjust the nitrogen concentration to about 160 ppm or more, and adjust the phosphorus concentration to about 20 PPm or more and adjust the tannin concentration. In order to check the above two inferences, the culture solution 1 to the culture solution 6 having the component composition of Fig. 4 are prepared. The composition of the culture solution 7 is the culture solution described in the literature 1. The component composition, and the component composition of the culture solution 8 is the component composition of the culture solution described in Document 2. The nitrogen concentration, the phosphorus concentration, the barium mass concentration, P/N and Si/N in each culture solution are respectively expressed in Fig. 5. The mass concentration of phosphorus and the concentration of strontium in the culture solution 1 are smaller than the above-mentioned inferential values. The concentration of nitrogen in the culture solution 1, the mass concentration of phosphorus, and the concentration of strontium are respectively 166 (ppm), l (ppm), 30 (ppm), while p/N, Si/N are 0.06 and 0.18, respectively. The phosphorus concentration of the culture solution 2 was adjusted to twice the concentration of the culture solution 1 (phosphorus mass concentration 1294913 degrees = 20 (ppm), p/n = 〇 12). The mass concentration of the culture solution 3 was adjusted to twice the concentration of the culture solution (矽 mass concentration = 60 (ppm), si/N = 0.36). The phosphorus concentration and the strontium mass concentration of the culture solution 4 were respectively adjusted to twice the culture solution 1 (phosphorus mass concentration = 20 (ppm), Ρ / Ν = 0.12, 矽 mass concentration = 60 (ppm), Si / N=〇.36). The mass concentration of the culture solution 5 was adjusted to 3 times that of the culture solution 2 (矽 mass concentration = 90 (ppm), si/N = 0.54). The mass concentration of the culture solution 6 was adjusted to 4 times that of the culture solution 2 (矽 mass concentration = 120 (ppm), si/N = 0.72). The mass concentration of phosphorus in culture medium 2-6, the mass concentration of strontium, p/N& Si/N, the mass concentration of phosphorus in the culture liquids 7 and 8 of the previous composition, the mass concentration of the mass, P/N, Si/ N is high. The third step is the relationship between the pH value and the amount of hydrolysis in the culture solution having a higher phosphorus concentration and a higher mass concentration. The concentration of sodium hydrogencarbonate (NaHc〇3), which is one of the components of the culture solution, was increased by 1 to change the pH of the culture solution 4 between 7.0 and 9.0. At the same time, the amount of hydrolysis produced in the culture solution 4 (the mass (kg) of the hydrolyzate produced per im3 of the solution was measured). During the period, the culture solution 4 was supplied with a component which was necessary to maintain life in the culture solution, and 3°/. The air of carbonation gas is used as a cultivating solution 4 for aeration and agitation. The results of the child test are shown in Figure 6. The solid line and the broken line in Fig. 6 show the change in the amount of hydrolysis obtained on different experimental days, respectively, and the results are slightly consistent. As the measurement was learned, when the pH of the culture solution 4 exceeded 8·5, the change in the amount of hydrolysis accelerated, and the amount of hydrolysis (precipitate amount) increased. The mouth of the culture liquid is more than 8 after 1294913: the sediment contains Chaetoceros, and the Chaetoceros no longer breeds. The fourth step is to determine the upper limit of the positive value of the culture solution. In this experiment, the pH of the sodium hydride and the 3% carbonation gas were adjusted, and the amount of σ & acid hydrogen was increased, and the pH of the solution was also increased, while the carbonation time was increased. ^ Plus 'Luo liquid heart pH is reduced. The carbon source and the carbonic acid gas supply to the Chaetoceros are used as a pH adjuster for the culture solution. The culture solution 1 (11 〇xl〇-3m3) is placed in a closed reactor set outdoors: the temperature is maintained below about 25 ° C, and the quantum of light is about 12 〇 0_ol/mVs · intensity <self & sunlight Irradiated on the culture solution. In this state, the first measurement was carried out by mixing the air culture agitated culture solution i with 3% carbonation gas, and the change in the concentration of the cells of the Chaetoceros in the culture medium 1 and the time. The second item was the addition of sodium bicarbonate (7 0xl03 and then air ventilated to see the mixed culture solution 1 to determine the time change of the concentration of the cells in the culture liquid i and the time change of the pH. The test results are shown in Fig. 8. The solid line in Fig. 8 is the result of the first measurement, that is, the time change of the pH of the culture solution 1 in the case of mixing with 3% carbonation gas under the action of sodium hydrogencarbonate. The dotted line is the second measurement, which means the time change of the pH of the culture solution 1 under the addition of sodium bicarbonate, only when air is ventilated. It is learned from the above measurement results that the culture medium is ventilated by air. Stirring, and adding sodium bicarbonate, when the kpH of the culture solution exceeds 8.5, the sinking hall is produced. At this time, the dinoflagellate is co-precipitated with the precipitate, and is agitated with air mixed with 3% carbonic acid gas without adding sodium bicarbonate. At the same time, the pH of the culture solution 1 gradually decreases. -15- 1294913 The third and fourth items are determined by the sister ^ ^. Also, when adding sodium bicarbonate to the culture solution, 'right* is mixed with 3% citrate. The stirring culture solution with , sa, and two can be set to a pH of 8.4 or less. It is necessary to prevent the precipitation from occurring and the co-precipitation of Chaetoceros. - As for the composition of the culture solution 1, the components other than the P/N or Si/N are the same as the components of the culture solution 2 to 6. Therefore, The solubility of the culture is the same as the solubility of other culture solutions. When other culture solutions are used, if the culture solution is agitated with air mixed with carbonation gas in the state of adding bicarbonate to the culture solution, the sink should be prevented. The fifth step is about the lower limit of p H of the culture solution and the appropriate addition and addition range of sodium bicarbonate. The quality of sodium bicarbonate which is one of the components of the culture medium is changed. Concentration, adjust the following 8 kinds of culture solution 1 to mix 3% carbonation air, agitate and stir the culture solution J. [l]0.02xl03 ppm^ [2]0.07xl〇3 ppm , [3]〇.14xl〇3 ppm , [4] 〇.28 xlO3 ppm, [5]0·56χ103 ppm, [6]1.OxlO3 ppm, [7]2〇χ1〇3 ppm, [8]7·〇χ 1〇3 ppm. Each culture medium ι prepared is subjected to a culture experiment of Chaetoceros, and the time change of the cell concentration and the time change of the pH are measured. · In order to ensure reproducibility, the above experiments are different. It is carried out four times a day. Figures 9 and 10 are the results of the first measurement. The first culture experiment uses a culture solution having the following three concentrations of sodium bicarbonate: [ι]〇·〇2χΐ〇3 ppm, [ 3] 0.14xl03 ppm, [6] l. 〇 xl03 ppm. Figure XI shows that XI, X2 and X3 are represented by [1]0·02χ103 ppm, [3]0·14χ103 ppm,[6]1·〇 Time variation of cell concentration of Chaetoceros cultivarum cultured in χ103 ppm of culture medium. Figure ι 〇 ΧΑ ΧΑ ΧΑ 2 and ΧΑ 3 respectively indicate [1] 〇 · 〇 2 χ 103 ppm, [3] 〇 · 14 χ 1 〇 3 ppm, [6] 1 · 〇χ 103 ppm of the pH of the culture solution 1 Variety. -16 - 1294913 Figures 11 and 12 are the results of the second measurement. The second culture experiment used a culture solution having the following four concentrations of sodium bicarbonate: [2] 〇〇 7xl 〇 3 ppm, [3] 0·14 χ 103 ppm, [4] 0·28 χ 103 ppm and [6] 1·〇χ1〇3 ppm. Y, Y2, Y3, and Y4 of Fig. u are represented by [2] 〇.〇7xi〇3 ppm, [3]〇.ΐ4 χΙΟ3 ppm, [4]0.28xl03 ppm and [6]1·〇χ1〇3 ppm The culture solution is changed in time of cell concentration of C. albicans. In Fig. 12, yab YA2, YA3, and YA4 respectively represent [2]0.07><10 ppm '[3]0·14χ103 ppm, [4]0·28 xlO3 ppm and [6]l.〇xl03 ppm The time of the pH of the culture solution 1 changes. Figures 13 and 14 show the results of the third measurement. The third culture test used four culture solutions with the following concentrations of hydrogen carbonate: [4] 〇.28χ103 ppm, [5]0.56xl03 ppm, [6]l.〇xl〇3 ppm and [7]2 ·〇χ1〇3 ppm. Z1, Z2, Z3, and Z4 shown in Fig. 13 are represented by [4] 〇 · 28 χ 103 ppm, [5] 0 · 56 x lO3 ppm, [6] l. 〇 xl03 ppm and [7] 2. 〇 xl 〇 3 ppm The time change of the concentration of the cells of the cultured Chaetoceros cultured in the culture solution 1. On the other hand, ZA1, ZA2, ZA3, and ZA4 in Fig. 14 represent [4]0·28χ103 ppm, [5]0.56x 103 ppm, [6]1·0 xlO3 ppm, and [7]2.0 xlO3 ppm of culture solution 1 The time of pH changes. Figures 15 and 16 are the results of the fourth measurement. The fourth culture experiment used a culture solution containing the following two concentrations of sodium bicarbonate: [6] 1.0x1 〇 3 ppm, [8] 7 · 〇χ 103 ppm. Wl and W2 of Fig. 15 show the time-dependent changes in the concentration of Chaetoceros cells cultured in the culture solution 1 of [6]1·〇χ1〇3 ppm, [8]7.〇xl〇3 ppm, respectively. On the other hand, WA1 and WA2 in Fig. 16 indicate the time change of [6] l_〇xl 〇 3 ppm, [8] 7·0 x lO3 ppm culture solution 1, respectively. The following results were obtained from the above measurement results. [1] In 0.02X 103 ppm of culture solution 1, the pH value decreased immediately after the start of the experiment, 1294913, and decreased to below 6.4 after about 25 hours, and the cell concentration was less than 3 cells/m3. [2] In the culture solution of 0.07X1G3 ppm, the pH is maintained above about 7.0 and below the range, and the cell concentration is up to 3χ1〇η cells~3. [3] In the culture of 〇.14xH)3 ppm, the pH value is maintained above about u and below about 7.4, while the cell concentration exceeds 4χ1〇π cells^3. [4] In 0.28X1G3 ppm of culture! The _ direct line is maintained at about 7.6 or less, and the cell concentration is above 4 χΐ〇 13 cells. [5] In the culture solution 1 of 0.56 Χ 103 ppm, the ρ Η value is maintained above about Μ and about 7.6 or less, and the cell concentration thereof is 4 < 1 〇 13 cells / ^ or more. [6] In l.〇xl〇3ppmi culture solution 1, which? The value of 1^ is maintained in the range of about 6.4 or more and about 7.9 or less, and the cell concentration thereof is 6χ1〇13 cells/melon 3 or more. [7] In the culture solution of 2.0x10ppm, the pH is maintained at about 7〇 or more and about 8.1 or less, and the cell concentration is 5χ1〇13 cells/m3 or more. [8] Medium in 7.0xl03ppm! The pH is maintained at about 6. 7 or more and about 8.1 or less, and the cell concentration is 3 χ 1 〇 13 cells/m 3 or more. Therefore, after preparing a culture solution 1 having a mass concentration of sodium hydrogencarbonate higher than 〇〇2xl〇3ppm or more, the mixture is aerated and stirred with air mixed with 3% carbonation gas, and the pH of the culture solution 1 is set to 6.4 or more, and the angle can be made. The cell concentration of Chaetoceros exceeds the upper limit of the concentration of Chaetoceros cells reached by the previous culture method (3χΐ〇π cells/m3).
至於培養液1之成分,相較於培養液2〜6之成分,除p/N -18- 1294913 及/或S i/N以外,其他成分則相同。因此,使用其他培養液 時,似可調製含有0·02χ103 ppm以上之碳酸氫鈉質量濃度之 培養液1後,以混合3%碳酸氣之空氣通氣攪拌該培養液丄, 使培養液1之pH值設定於6 ·4以上’則可達成較先前培養方 法所達到之角毛藻細胞濃度上限值(3 X 1〇13細胞/m3)以上。 由上述4次測定結果獲知,使用培養液i〜6培養角毛藻 時’若將培養液之pH值設定於6.4以上,8·4以下範圍,則 可穩定培養角毛蕩。為符合該條件,可行方法之一為調製 具有碳酸氫鈉質量濃度高於0·02χ103 ppm之培養液,而以混 合3%碳酸氣之空氣,通氣攪拌培養液。 將培養液1〜6之pH值設定於6 ·4以上,則可使角毛藻細胞 濃度高於以先前培養方法培養時之上限值。此外,將培養 液1〜6之pH值設定於8.4以下,則可抑制因ρΗ昇高而產生水 角f引起之角毛藻之共沉’由此可防止角毛藻之繁殖降低。 【實施方式】 以下,根據上述條件,以實施例i-U詳述,以高濃度穩 定之碎藻培養方法。 (實施例1) 對如圖7之實驗用扁型培養瓶11(容量丨·5χ 1〇-3 m3),放進 培養液1(1·5χ10·3 m3),添加碳酸氫鈉,使碳酸氫鈉之質量 濃度為l.OxlO3 ppm。然後將規定量之角毛藻接種於該培養 液1。將培養液之溫度維持於約25t〜約351,並利用日光 燈,以光量子量約200 pm〇i/m2/s強度之光線照射培養液1, 在该狀態下,藉著貫通瓶Π之栓12之玻璃管13,送進混合 1294913 3%¾¾氣之空氣於培養液1 ’進行角毛藻之培養實驗。並 分別測定培養液1之角毛藻細胞濃度之時間變化及pH之時 間變化。 (實施例2) 將培養液2(1.5XI(Γ3 m3)放進實驗室内之扁型培養瓶u, 添加碳酸氫鈉,使碳酸氫鈉之質量濃度為1 〇x 1〇3 ppm。然 後對培養液2接種規定量(與實施例1同量)之角毛藻以與實 施例1略同條件(培養液溫度:約25°C〜約35°C,光量子量: 約200 pmol/m2/s,用混合3%碳酸氣之空氣通氣揽拌)實施 培養實驗,分別測定培養液2之角毛藻細胞濃度之時間變化 及pH之時間變化。 (實施例3) 將培養液3(1.5x1 (T3 m3)放進實驗室内之扁型培養瓶11, 添加碳酸氫鈉,使碳酸氫鈉之質量濃度為l.OxlO3 ppm。然 後對培養液3接種規定量(與實施例丨同量)之角毛藻,以與實 施例1略同條件(培養液溫度:約25°C〜約35°C,光量子量: 約200 pni〇l/m2/s,用混合3%碳酸氣之空氣通氣攪拌)實施 角毛漢之培養實驗,並分別測定培養液3之角毛藻細胞濃度 之時間變化及pH之時間變化。 (實施例4) 將培養液4(1 ·5XI(T3 放進實驗室内之扁型培養瓶u, 添加碳酸氫鈉,使碳酸氫鈉之質量濃度達l.OxlO3 ppm。然 後對培養液4接種規定量(與實施例1同量)之角毛藻,以與實 施例1略同之條件(培養液溫度:約25°C〜約35°C,光量子 1294913 f ·約200 gmol/m2/s,以混合3%碳酸氣之空氣通氣授拌) 爲施角毛藻之培養實驗,為分別測定培養液4之角毛藻細胞 ;辰度之時間變化及pH之時間變化。 圖1 7表不實施例1〜4之角毛藻細胞濃度之時間變化圖。圖 1 7中之C 1 ’ C2 ’ C3 ’ C4分別表示以培養液1,2,3,4培養 之角毛藻之細胞濃度之時間變化,而圖丨7中之A則係對各培 養液補給追肥成分(含於培養液之氮、磷、矽、維生素類、 微量礦物質類)之時間。 圖18表示實施例1〜實施例*之pH之時間變化圖。圖18之 D1 D2 ’ D3 ’ D4係分別表示培養液1,2,3,*之pH之時 間變化。 由上述測定結果獲知: 對培養液1(P/N=0.06,Si/N=0.18)將矽量設定2倍之培養 液 3(P/N=0.06,Si/N=〇_36)之細胞濃度(約 8〇xl〇13 細胞〜3) 问於培養液1之角毛藻細胞濃度(約6 〇x l〇i3細胞/m3)。 對培養液1(P/N=0.06,Si/N=0.18)分別將磷量及矽量設定 為2倍之培養液4(P/N:=(M2,Si/N=〇·36),其細胞濃度(約7加 細胞/m )鬲於培養液i之角毛藻細胞濃度(約6 〇x 1〇u)細 胞 /m3。 培養液1-4之各pH係維持於6·4以上而8·5以下範圍,亦即 維持於約7.5以上’而約8.5以下範圍。 至於實驗4之培養液4之細胞濃度測定,由於實驗中之混 u蛟酸氣之空氣之供給可能不充足,其數據或許與實驗稍 有差距。 -21 - 1294913 性,另以與實施例1-4 ’測足培養液1 - 4之角 為檢討實施例1-4之測定結果之再現性,另 之條件,且不補給追肥成分之下培養,測定 毛藻細胞濃度之時間變化及pH之時間變化、 圖I9係實施再現性實驗時之培養液i 1 一4之角毛藻細胞濃As for the component of the culture solution 1, the components other than the components of the culture solution 2 to 6 were the same except for p/N -18-1294913 and/or S i/N. Therefore, when using another culture solution, it is possible to prepare a culture solution 1 containing a mass concentration of sodium bicarbonate of 0. 02 χ 103 ppm or more, and then agitating the culture solution with a mixture of 3% carbonation gas to adjust the pH of the culture solution 1. When the value is set to 6.4 or more, the upper limit of the concentration of Chaetoceros cells (3 X 1〇13 cells/m3) or more which is achieved by the previous culture method can be achieved. From the results of the above-mentioned four measurements, it was found that when the culture liquid i to 6 was used to culture the Chaetoceros, the pH of the culture solution was set to 6.4 or more and 8.4 or less. In order to meet this condition, one of the feasible methods is to prepare a culture solution having a sodium bicarbonate mass concentration higher than 0. 02 χ 103 ppm, and mixing the culture solution with a mixture of 3% carbonation gas. When the pH of the culture solution 1 to 6 is set to 6.4 or more, the cell concentration of Chaetoceros can be made higher than the upper limit when cultured by the prior culture method. Further, by setting the pH of the culture liquids 1 to 6 to 8.4 or less, it is possible to suppress the co-precipitation of the Chaetoceros caused by the water angle f due to the increase in pH, thereby preventing the growth of Chaetoceros from decreasing. [Embodiment] Hereinafter, the algae cultivation method which is stabilized at a high concentration will be described in detail in the examples i-U in accordance with the above conditions. (Example 1) The flat culture flask 11 (capacity 丨·5χ 1〇-3 m3) for the experiment as shown in Fig. 7 was placed in the culture solution 1 (1·5χ10·3 m3), and sodium hydrogencarbonate was added to make carbonic acid. The mass concentration of sodium hydrogen is 1.0 OxlO3 ppm. Then, a predetermined amount of Chaetoceros was inoculated to the culture solution 1. The temperature of the culture solution is maintained at about 25t to about 351, and the culture solution 1 is irradiated with light having a light quantum amount of about 200 pm〇i/m2/s by a fluorescent lamp. In this state, the plug 12 is passed through the bottle. The glass tube 13 is fed with a mixture of 1294913 3% 3⁄43⁄4 of air in the culture solution 1 'C. The time change of the concentration of Chaetoceros cells in the culture solution 1 and the time change of the pH were measured. (Example 2) The culture solution 2 (1.5XI (Γ3 m3) was placed in a flat culture flask u in a laboratory, and sodium hydrogencarbonate was added so that the mass concentration of sodium hydrogencarbonate was 1 〇 x 1 〇 3 ppm. Then The culture solution 2 was inoculated with a predetermined amount (the same amount as in Example 1) to have the same conditions as in Example 1 (culture temperature: about 25 ° C to about 35 ° C, photoquantity: about 200 pmol/m 2 ) /s, the air culture was mixed with 3% carbonation gas to carry out a culture experiment, and the time change of the concentration of the cells of the cultured liquid 2 and the time change of the pH were respectively measured. (Example 3) The culture liquid 3 (1.5) X1 (T3 m3) is placed in the flat culture flask 11 in the laboratory, sodium bicarbonate is added, so that the mass concentration of sodium bicarbonate is 1.0 OxlO3 ppm. Then, the culture solution 3 is inoculated with a prescribed amount (the same amount as the embodiment) ) C. elegans, in the same conditions as in Example 1 (culture temperature: about 25 ° C ~ about 35 ° C, quantum of light: about 200 pni〇l / m2 / s, mixed with 3% carbon dioxide air The aeration experiment was carried out, and the time change of the concentration of the cells of the cultured liquid 3 and the time change of the pH were measured. The culture solution 4 (1 · 5XI (T3 is placed in a flat culture flask in the laboratory, sodium bicarbonate is added, so that the mass concentration of sodium bicarbonate is 1.0 OxlO3 ppm. Then the culture solution 4 is inoculated with a prescribed amount ( The same amount as in Example 1 was carried out under the same conditions as in Example 1 (culture temperature: about 25 ° C to about 35 ° C, photon 1294913 f · about 200 gmol / m 2 / s, to mix 3% carbonation gas air ventilating) For the culture experiment of C. cerevisiae, the C. albicans cells of the culture solution 4 were measured separately; the time change of the time and the time change of the pH. Figure 1 7 shows Example 1 The time change of the concentration of Chaetoceros cells in ~4. The C 1 'C2 'C3 'C4 in Figure 1 7 shows the time change of the cell concentration of Chaetoceros sinensis cultured in culture medium 1, 2, 3, 4, respectively. In the case of Fig. 7, A is the time for supplying the topdressing component (nitrogen, phosphorus, strontium, vitamins, and trace minerals contained in the culture solution) to each culture solution. Fig. 18 shows the results of Examples 1 to 4. The time change diagram of pH. D1 D2 'D3 ' D4 of Fig. 18 indicates the time change of the pH of the culture solution 1, 2, 3, *, respectively. The results were ascertained: For the culture solution 1 (P/N=0.06, Si/N=0.18), the cell concentration of the culture solution 3 (P/N=0.06, Si/N=〇_36) was set to 2 times. About 8〇xl〇13 cells ~3) Ask about the concentration of C. elegans cells in culture medium 1 (about 6 〇xl〇i3 cells/m3). For culture medium 1 (P/N=0.06, Si/N=0.18) The amount of phosphorus and the amount of strontium were respectively set to 2 times the culture solution 4 (P/N:=(M2, Si/N=〇·36), and the cell concentration (about 7 cells/m) was immersed in the culture solution i. Cell concentration of Chaetoceros (about 6 〇 x 1〇u) cells/m3. The pH of each of the culture solutions 1-4 is maintained in the range of 6.4 or more and 8.5 or less, i.e., maintained at a range of about 7.5 or more and about 8.5 or less. As for the measurement of the cell concentration of the culture solution 4 of Experiment 4, since the supply of the air of the mixed gas in the experiment may not be sufficient, the data may be slightly different from the experiment. -21 - 1294913, and the reproducibility of the measurement results of Example 1-4 was examined in the same manner as in Example 1-4 'Measurement of the culture medium 1 - 4, and the conditions were not raised under the top dressing ingredients. , measuring the time change of the concentration of the cells of the hairy algae and the time change of the pH, and the culture medium i 1 to 4 in the reproducibility experiment in FIG.
之pH。 由上述測定結果獲知: 將磷T設定為培養液1(ρ/Ν=〇·〇6,si/N=0.18)之2倍之培 養夜2(Ρ/Ν=0·12 ’ Si/N=〇.l8)之角毛、藻細胞濃度高於培養液 1之角毛藻細胞濃度。 將矽量設定為培養液1(Ρ/Ν=〇·〇6 , Si/N=〇18)之2倍之培 養液3(P/N=G.G6,Si/N’6)之角毛藻細胞濃度高於培養液 1之角毛藻細胞濃度。 將磷量及矽量分別設定為培養液1(1>/1^=〇.〇6,Si/N=〇 i8) 艾2倍之培養液4(P/N==〇12,Si/N=〇.36)之角毛藻細胞濃度 馬於培養液1之角毛藻細胞濃度。 培養液4之角毛藻細胞濃度高於培養液2,3之細胞濃度。 培養液1-4之各pH係維持於6.4以上,8·5以下範圍内,亦 即維持於約7 · 4以上至約8 · 〇以下範圍。 由上述實施例1 _4結果可推論,以含培養液1之2倍以上嶙 I及/或含培養液1之2倍以上之矽量之培養液作為追肥培 1294913 養角毛藻時,角毛藻之細胞濃度將達約6 〇xl〇n細胞/m3以 上。 為證實上述推論,以含培養液1之2倍磷量之培養液2,含 _ 培養液1之2倍磷量及2倍矽量之培養液4,及含培養液丨之2 · 倍% f及3倍矽量之培養液5作為追肥,分別培養角毛藻。 (實施例5) 如同實施例2,將培養液2(1.5X10_3 m3)放進扁型培養瓶 1 1 ’添加後酸氫鈉,使碳酸氫鈉質量濃度為1 〇 xlO3 ppm。 然後對培養液2接種規定量(與實施例2同量)之角毛藻,以與 # 實施例2略同條件(培養液溫度:約以它〜約35χ:,光量子 量:約200 (amol/mVs,用混合3%碳酸氣之空氣通氣攪拌) 實施角毛藻培養實驗,並分別測定培養液2之角毛藻細胞濃 度之時間變化及pH之時間變化。 (實施例6) 如同實施例4,將培養液4(15><1〇-31113)放進扁型培養瓶 Π,添加碳酸氫納,使碳酸氫鈉之質量濃度為1·〇χ1〇3 ppm。 然後對培養液4接種規定量(與實施例5同量)之角毛藻,以與馨 實施例5略同之條件(培養液溫度··約25Ό〜約35〇c,光量子 里·約200 Kmol/m2/s,用混合3%碳酸氣之空氣通氣攪拌) 實施角毛藻培養實驗,並分別測定培養液4之角毛藻細胞濃 度之時間變化及pH之時間變化。 (實施例7) 將培養液5(1·5χ1(Γ3 m3)放進扁型培養瓶!〗,添加碳酸氫 麵,使碳酸氫鈉之質量濃度為l.〇xl〇3ppm。然後對培養液5 -23- 1294913 接種規定量(與實施例5同量)之角毛藻,以與實施例5略同條 件(培養液溫度:約25它〜約35 t,光量子量:約2二 叫〇‘/^實施角毛藻培養實驗’並分別測定培養液5之角 毛藻細胞濃度之時間變化及pH之時間變化。 圖21為實施例5-7之角毛藻細胞濃度之時間變化圖。圖21 中之G1 G2 G3刀力彳表不以培養液2,4,5培養之角毛藻 細胞濃度之時間變化。而圖21中之八為對各培養液補給追肥 成分(含於培養液之氮m生素類及微量礦物質 之時間。 / 圖22為實施例之PH之時間變化圖。圖22中之HI,H2, H3分別為培養液2, 4, 5之阳之時間變化,而圖η中之則 係表示實驗室内室溫之時間變化。H5表示培養液溫度之時 間變化。 由上述測定結果獲知: 將矽里设定為培養液2(ρ/ν=〇·12, Si/N=0.18)之2倍之培養 液,P/N=〇. U,Si/N=0.36)之角毛藻細胞濃度(9.〇χ丨〇u細胞 /m3)高於培養液2之角毛藻細胞濃度。 知矽臺设定為培養液2(ρ/Ν=〇·ΐ2, Si/N=0.18)之3倍之培養 液5(Υ/Ν==0_12,Si/N=0·54)之角毛、藻細胞濃度(約9·〇χ1〇13細 胞/m3)高於培養液2之角毛藻細胞濃度。 。養液4與培養液5之角毛藻細胞濃度差距並不大。 私養液2,4,5之各pH係維持於6·4以上,8·5以下範圍, 亦即維持於約7.4以上,約8.2以下範圍。 由上述實驗結果推論,以含培養液2之2倍以上矽量之培 -24- 1294913 養液培養角毛藻時,角毛藻細胞濃度將可達約8·〇χ1〇ΐ3細胞 /m3以上。 為證實該推論,使用培養液2,4,5以及培養液6,以與 實施例5同一條件再次實施培養實驗,分別測定培養液2, 4,5,6之角毛藻細胞濃度之時間變化及pH之時間變化。 圖23為再培養實驗時之角毛藻細胞濃度之時間變化圖。 圖23之II,12,13,14表示以培養液2,4,5,6培養之角毛 藻細胞濃度之時間變化。 圖24為再培養實驗時之pH之時間變化圖。圖24之Ji,J2, J3 ’ J4表示培養液2,4,5,6之pH。圖24之J5表示實驗室 内之室溫之時間變化,而J 6則表示培養液溫度之時間變化。 由上述測定結果獲知: 將矽量設定為培養液2(p/n=0.12, Si/N=0.18)之2倍之培養 液4(Si/N=0·36)所得之角毛藻細胞濃度(約ι·〇χ1〇η細胞/爪3) 高於培養液2所得之角毛藻細胞濃度。 將矽量設定為培養液2(Ρ/Ν=0·12, Si/N=0.18)之3倍之培養 液5(Si/N=0·54)所得之角毛藻細胞濃度(約9,〇xl〇i3細胞/m3) 高於培養液2所得之角毛藻細胞濃度。 將矽量設定為培養液2(Ρ/Ν=0·12, Si/N==(U8)之4倍之培養 液6(Si/N=0·72)所得之角毛藻細胞濃度(約1·〇χ1〇14細胞/m3) 高於培養液2所得之角毛藻細胞濃度。 培養液4之角毛藻細胞濃度,相較於培養液5,6,並無大 幅差距。 培養液2,4,5,6之各pH均維持於6·4以上,8.5以下範 -25 - 1294913 圍’亦即維持於約7·3以上,8.1以下範園。 由上述貝施例5-7之實驗結果可知,倘使用選自培養液4_6 中任培養液培養角毛藻,則可使角毛藻細胞濃度增加至 、勺8·0 1〇細胞/m3以上。換言之,使用其Ρ/Ν為0.12以上及’ /N為0.36以上〈培養液培養角毛藻時,其角毛蕩細胞濃度 將增加至約8.OxlO13細胞/m3以上。 士其次,為檢討上述培養條件(Ρ/ΝΜ·12&8ί/ΝΜ·36)於連 續培養時能否在室内及戶外仍可成立,使用培養液4及培養 液6,實施如下實施例84 〇之實驗。 鲁 (實施例8) ,對汉万、實^至内之爲型培養瓶u,放進含氮(166叩瓜), 磷(20卯叫及矽(60卯111)之培養液4(1.5><1〇_31113),添加碳8 氫納’使碳酸氫鋼之質量濃度為UxW ppm。然後對該土 養液4接種規定量之角毛藻,以與實施例1略同之條件(培^ 溫度:約2穴〜約饥,光量子量:約2〇〇 μιη〇ι/πι2/3,❸ 混合3%碳酸氣之空氣通氣攪拌)實施角毛藻培養實驗,並分 別測定培養液4之角毛藻細胞濃度之時間變化及ρΗ之時間 變化。pH. It is known from the above measurement results that the phosphorus T is set to 2 times the culture night of the culture solution 1 (ρ/Ν=〇·〇6, si/N=0.18) 2 (Ρ/Ν=0·12 'Si/N=角.l8) The concentration of horn cells and algae cells is higher than that of culture medium 1 . Set the amount of sputum to the horn of the culture solution 3 (P/N=G.G6, Si/N'6) twice the culture solution 1 (Ρ/Ν=〇·〇6, Si/N=〇18) The algal cell concentration is higher than the C. elegans cell concentration in the culture solution 1. The amount of phosphorus and the amount of strontium were respectively set to the culture solution 1 (1>/1^=〇.〇6, Si/N=〇i8) Ai 2 times the culture solution 4 (P/N==〇12, Si/N = 〇.36) The concentration of Chaetoceros cells in the culture medium 1 is the concentration of Chaetoceros cells. The concentration of C. albicans cells in the culture solution 4 was higher than the cell concentration of the culture solution 2, 3. The pH of each of the culture solutions 1-4 is maintained at 6.4 or more, and is in the range of 8.5 or less, i.e., maintained in the range of about 7.4 or more to about 8 Å or less. From the results of the above Example 1 _4, it can be inferred that when the culture medium containing more than 2 times of the culture solution 1 and/or 2 times or more of the culture solution 1 is used as the top dressing 1294913, the horn hair The cell concentration of the algae will be above about 6 〇xl〇n cells/m3. In order to confirm the above inference, the culture solution 2 containing 2 times the amount of phosphorus in the culture solution 1 and the culture solution 4 containing 2 times the amount of phosphorus and 2 times the amount of the solution, and 2 % times the volume of the medium containing the solution F and 3 times the amount of the culture solution 5 as a top dressing, respectively cultured Chaetoceros. (Example 5) As in Example 2, the culture solution 2 (1.5×10 −3 m 3 ) was placed in a flat culture flask 1 1 ' After adding sodium hydrogen hydride, the mass concentration of sodium hydrogencarbonate was 1 〇 x 10 3 ppm. Then, the culture solution 2 was inoculated with a predetermined amount (the same amount as in Example 2) of C. elegans in the same condition as #Example 2 (culture temperature: about ~5 χ:, quantum amount of light: about 200 (amol) /mVs, aerated with a mixture of 3% carbonation gas, aerated) The Chaetoceros culture experiment was carried out, and the time change of the concentration of Chaetoceros cells in the culture solution 2 and the time change of the pH were respectively measured. (Example 6) 4. Place the culture solution 4 (15 ><1〇-31113) in a flat culture flask, and add sodium bicarbonate so that the mass concentration of sodium hydrogencarbonate is 1·〇χ1〇3 ppm. Then, the culture solution 4 Inoculation of a specified amount (the same amount as in Example 5) of Chaetoceros sinensis, in the same condition as in the scent of Example 5 (the temperature of the culture solution was about 25 Ό to about 35 〇 c, and the quantum of light was about 200 Kmol/m 2 /s). The mixture was ventilated with air mixed with 3% carbonic acid gas to carry out a culture experiment of Chaetoceros sinensis, and the time change of the concentration of Chaetoceros cells in the culture solution 4 and the time change of the pH were respectively determined. (Example 7) The culture solution 5 ( 1·5χ1 (Γ3 m3) put into the flat culture bottle!〗, add the hydrogen carbonate surface, so that the mass concentration of sodium bicarbonate is l. Xl 〇 3 ppm. Then, the culture solution 5 -23-1294913 was inoculated with a prescribed amount (the same amount as in Example 5) of Chaetoceros, with the same conditions as in Example 5 (culture temperature: about 25 it ~ about 35 t, The quantum of light: about 2 〇 〇 ' / ^ carried out the culture of Chaetoceros ' and the time change of the concentration of Chaetoceros cells in culture medium 5 and the time change of pH. Figure 21 is the angular hair of Example 5-7 The time change of the algae cell concentration. The G1 G2 G3 knife force in Figure 21 does not change the cell concentration of C. elegans cultured in culture medium 2, 4, and 5. The eighth in Figure 21 is for each culture solution. Replenishing the top dressing component (the time of the nitrogen methane and the trace mineral contained in the culture solution. / Figure 22 is the time change diagram of the PH of the example. The HI, H2, H3 in Fig. 22 are the culture solution 2, 4 respectively. The time of the yang of 5 changes, while the figure η represents the time change of the room temperature in the laboratory. H5 represents the time change of the temperature of the culture solution. It is known from the above measurement results: the sputum is set as the culture solution 2 ( ρ / ν = 〇 · 12, Si / N = 0.18) twice the culture solution, P / N = 〇. U, Si / N = 0.36) Chaetoceros cell concentration (9. 〇χ丨〇u cells/m3) are higher than the concentration of Chaetoceros cells in the culture solution 2. The cultivar is set to culture 3 times the culture solution 2 (ρ/Ν=〇·ΐ2, Si/N=0.18) The concentration of horns and algae cells (about 9·〇χ1〇13 cells/m3) of liquid 5 (Υ/Ν==0_12, Si/N=0·54) was higher than that of culture medium 2. The difference between the concentration of the cultured liquid 4 and the culture liquid 5 is not large. The pH of each of the private liquids 2, 4, and 5 is maintained at 6.4 or higher and 8.5 or less, that is, maintained at about 7.4 or higher. , about 8.2 or less. It is inferred from the above experimental results that the cell concentration of C. cerevisiae can reach about 8·〇χ1〇ΐ3 cells/m3 or more when the cultured C. elegans is cultured with the culture medium containing 2 times or more of the broth 2-24. . In order to confirm the inference, the culture liquids 2, 4, 5 and the culture liquid 6 were used, and the culture experiment was again carried out under the same conditions as in Example 5, and the time change of the concentration of the cells of the cultured liquid 2, 4, 5, and 6 was measured. And the time of pH changes. Figure 23 is a graph showing the time change of the concentration of Chaetoceros cells in the re-culture experiment. II, 12, 13, and 14 of Fig. 23 show temporal changes in cell concentration of Chaetoceros cultured in culture medium 2, 4, 5, and 6. Figure 24 is a graph showing the time change of pH at the time of the re-culture experiment. Ji, J2, J3' J4 of Fig. 24 indicate the pH of the culture liquids 2, 4, 5, and 6. J5 of Fig. 24 indicates the time change of the room temperature in the laboratory, and J 6 indicates the time change of the temperature of the culture solution. From the above measurement results, it was found that the concentration of sputum was determined by setting the amount of sputum to the culture solution 4 (Si/N = 0.36) twice the culture solution 2 (p/n = 0.12, Si/N = 0.18). (About ι·〇χ1〇η cells/claw 3) The concentration of Chaetoceros cells obtained from the culture solution 2 was higher. Set the amount of sputum to the concentration of Chaetoceros cells obtained by the culture solution 5 (Si/N = 0.54) which is 3 times the culture solution 2 (Ρ/Ν=0·12, Si/N=0.18) (about 9, 〇xl〇i3 cells/m3) is higher than the concentration of Chaetoceros cells obtained in the culture solution 2. Set the amount of sputum to the concentration of Chaetoceros cells obtained from the culture solution 2 (Ρ/Ν=0·12, Si/N==(U8) 4 times the culture solution 6 (Si/N=0.72). 1·〇χ1〇14 cells/m3) The concentration of Chaetoceros cells obtained from the culture solution 2. The concentration of Chaetoceros cells in the culture solution 4 was not significantly different from that of the culture solutions 5 and 6. Culture medium 2 The pH of each of 4, 5, and 6 is maintained above 6.4, and the range of 8.5 or less is -25 - 1294913. It is maintained at about 7.3 or above, and is below 8.1. The above-mentioned shell examples 5-7 As a result of the experiment, it can be seen that if the culture medium of the culture medium 4_6 is used to culture the Chaetoceros, the cell concentration of the Chaetoceros can be increased to be more than 8·10 1 cells/m3. In other words, the Ρ/Ν is used. 0.12 or more and '/N is 0.36 or more. When the culture medium is cultured, the concentration of horn cells will increase to about 8.OxlO13 cells/m3 or more. In order to review the above culture conditions (Ρ/ΝΜ·12& 8 ί / ΝΜ · 36) Whether it can be established indoors or outdoors during continuous culture, using the culture solution 4 and the culture solution 6, the experiment of the following Example 84 is carried out. Lu (Example 8), for Han Wan, Shi ^ In the type of culture flask u, put nitrogen (166 叩 melon), phosphorus (20 卯 and 矽 (60 卯 111) broth 4 (1.5 >< 1 〇 _31113), add carbon 8 hydrogen Na's the mass concentration of the bicarbonate steel is UxW ppm. Then the soil nutrient solution 4 is inoculated with a specified amount of Chaetoceros, in the same condition as in Example 1 (cultivation temperature: about 2 points ~ about hunger, light quantum Amount: about 2 〇〇μιη〇ι/πι2/3, ❸ mixed 3% carbonation gas air aeration and stirring) to carry out the culture of C. cerevisiae, and determine the time change of the concentration of C. elegans cells in culture medium 4 and Change of time.
在測定過程中,於角毛藻細胞濃度達約6〇χΐ〇13細胞址3 以上時,取出培養液4之約2/3量溶液,而以溶解seaufe之 人造海水取代。該人造海水溶解含氮、磷、矽、維生素等 之追肥成分則成追肥用培養液,作為補給於扁型培養瓶u 内之培養液4用。該操作稱為半批連續培養。 在半批連續培養之過程中,從培養液4抽出約2/3量溶液 -26- 1294913 後’而尚未補給追肥用培養液之前’分別測定该培養液4 (以 下簡稱追肥前培養液4a)之氮量、磷量及矽量’然後分別計 算該追肥前培養液切所含氮量、磷量及矽量與接種角毛藻 前之培養液(初期培養液)4所含氮量、磷量及矽量之差距。 至於初期培養液4所含氮量、磷量及矽量則分別為166 ppm、20 ppm、60Q ppm 0 根據上述計算而得之氮、磷及矽之各量差距,將經調整 氮、磷及矽之追肥用培養液補給於追肥前培養液4a,使追 肥前之培養液4a中之P/N及Si/N與初期培養液4之Ρ/Ν(=0·12) 及Si/N ( = 〇_36)—致。經該操作於補給後,該培養液4之Ρ/Ν 及Si/N則可保持一定(參照圖25)。 反覆半批連續培養中,則分別測定培養液4之角毛藻細胞 濃度之時間變化及pH之時間變化,據以計算角毛藻每ixl04 細胞所耗用之氮量、磷量及矽量。 (實施例9) 對實驗室内之扁型培養瓶11,放進含氮(166 ppnl),磷(20 ppm)及石夕(120 PPm)之培養液6(1·5χ1(Τ3 m3),添加碳酸氫 鋼’使碳酸氫鈉之質量濃度為1·〇χ1〇3 ρριη。然後對培養液6 接種規定量(同實驗例8)之角毛藻,以與實施例8略同之條件 (培養液溫度:約25°C〜約35°C,光量子量:約200 pmol/m2/s, 以混合3%碳酸氣之空氣通氣攪拌)實施角毛藻培養實驗(半 批培養連續培養)。中間分別測定培養液6之角毛藻細胞濃度 之時間變化及pH之時間變化。計算角毛藻每1><1〇4細胞所耗 用之氮量、鱗量及珍量。 -27- 1294913 圖26係實施例8及9之角毛藻細胞濃度之時間變化圖。圖 26之K1及K2表示以培養液4、6培養之角毛藻細胞濃度。圖 26之A1表示對各培養液第一次補給追肥成分(氮、磷、矽、 維生素類及礦物質類)之時間。此時,由於角毛藻細胞濃度 尚未達6.0x1013細胞/m3,因此,由各培養液抽取之量未達 全量之約2/3。圖26之A2〜7則分別表示角毛藻細胞濃度達 6.OxlO13細胞/m3時,由各培養液抽取全量之約2/3之溶液, 補給追肥用培養液之時間。 圖27係實施例8及9之pH之時間變化圖。圖27之LI、L2表 示培養液4、6之pH。 培養液4、6之各補給時間之角毛藻氮耗用量,角毛藻之 全體氮耗用量及每單細胞之角毛藻之全體氮耗用量,係依 下式計算: NCOMai=NFIR-NREMAi NCOMA2=NFIR+NADDai-NREMa2 NCOMa3=NREMa2+NADDa2-NREMA3 NCOMa4=NREMa3+NADDA3-NREMa4 ncomA5=nremA4+naddA4-nremA5 NCOMa6=NREMa5+NADDa5-NREMa6 NCOMa7=NREMa6+NADDa6-NREMa7During the measurement, when the cell concentration of C. cerevisiae was about 6 〇χΐ〇 13 cell site 3 or more, about 2/3 of the solution of the culture solution 4 was taken out, and it was replaced with artificial seawater which dissolved seaufe. The artificial seawater dissolves the topdressing component containing nitrogen, phosphorus, strontium, vitamins, and the like into a dressing culture liquid, and is used as a culture liquid 4 which is supplied to the flat culture bottle u. This operation is called semi-batch continuous culture. In the course of a half batch of continuous culture, about 2/3 of the solution -26-1294913 is extracted from the culture solution 4, and the culture solution 4 is measured before the culture solution for the top dressing is not added (hereinafter referred to as the pre-dressing culture solution 4a). The amount of nitrogen, the amount of phosphorus and the amount of strontium are then calculated. The nitrogen content, the amount of phosphorus and the amount of strontium before the cultivation of the pre-fertilized culture solution and the nitrogen content and phosphorus of the culture medium (initial culture solution) before the inoculation of Chaetoceros sinensis are respectively calculated. The difference between quantity and quantity. As for the amount of nitrogen, phosphorus and strontium in the initial culture solution 4, 166 ppm, 20 ppm, and 60 Q ppm, respectively. The difference in nitrogen, phosphorus and strontium obtained from the above calculations will be adjusted for nitrogen and phosphorus. The cultivating solution for topdressing is supplemented with pre-dressing culture solution 4a, so that P/N and Si/N in the culture solution 4a before top dressing and 初期/Ν (=0·12) and Si/N in the initial culture solution 4 ( = 〇_36). After the operation, the enthalpy/Ν and Si/N of the culture solution 4 can be kept constant (see Fig. 25). In the repeated half-batch continuous culture, the time change of the concentration of Chaetoceros cells in the culture solution 4 and the time change of the pH were measured, respectively, and the amount of nitrogen, phosphorus and strontium consumed by each ixl04 cell of Chaetoceros gracilis was calculated. (Example 9) For the flat culture flask 11 in the laboratory, a culture solution 6 (1·5χ1 (Τ3 m3) containing nitrogen (166 ppnl), phosphorus (20 ppm) and Shi Xi (120 PPm) was placed. The hydrogen carbonate steel was added to make the mass concentration of sodium hydrogencarbonate 1·〇χ1〇3 ρριη. Then, the culture solution 6 was inoculated with a predetermined amount (the same as Experimental Example 8), to the same conditions as in Example 8 ( The temperature of the culture solution: about 25 ° C to about 35 ° C, the quantum of light: about 200 pmol / m 2 / s, agitated with air mixed with 3% carbonation gas) to carry out the culture of Chaetoceros (continuous culture of half batch culture). The time change of the concentration of Chaetoceros cells in the culture solution 6 and the time change of the pH were measured in the middle, and the amount of nitrogen, the amount of scale, and the amount of nitrogen consumed by each of the 1>1〇4 cells were calculated. 1294913 Fig. 26 is a graph showing the time change of the concentration of Chaetoceros cells in Examples 8 and 9. K1 and K2 in Fig. 26 indicate the concentration of Chaetoceros cells cultured in the culture solutions 4 and 6. A1 of Fig. 26 indicates the respective culture solutions. The time to replenish the topdressing ingredients (nitrogen, phosphorus, antimony, vitamins and minerals) for the first time. At this time, the cell concentration of Chaetoceros has not reached 6.0x10. 13 cells/m3, therefore, the amount extracted from each culture solution is less than about 2/3 of the total amount. A2 to 7 of Fig. 26 respectively indicate that the cell concentration of C. cerevisiae is 6.OxlO13 cells/m3, respectively, from each culture solution. A total of about 2/3 of the solution was taken and the time for the dressing culture solution was replenished. Fig. 27 is a graph showing the time change of the pH of Examples 8 and 9. LI and L2 of Fig. 27 indicate the pH of the culture solutions 4 and 6. The nitrogen consumption of the algae in the replenishment time of 4 and 6 , the total nitrogen consumption of the horned algae and the total nitrogen consumption of the algae of the single cell are calculated according to the following formula: NCOMai=NFIR- NREMAi NCOMA2=NFIR+NADDai-NREMa2 NCOMa3=NREMa2+NADDa2-NREMA3 NCOMa4=NREMa3+NADDA3-NREMa4 ncomA5=nremA4+naddA4-nremA5 NCOMa6=NREMa5+NADDa5-NREMa6 NCOMa7=NREMa6+NADDa6-NREMa7
Nall4 丨化 7(NCOMAi/CELLAi)Nall4 丨化 7 (NCOMAi/CELLAi)
上開各式中之 NCOMAi,NFIR,NREMAi,NADDAi, NCOMunit,CELLAi及NALL分別代表下列之量。NCOMAi係 角毛藻於補給時間A(i-l)〜Ai之間耗用之氮量(ppm),NFIR 1294913 係初期培養液中之氮量(ppm),NREMAi係於補給時間^ 時,殘留於培養液之氮量(ppm),胸〜係於補給時間μ 時補給之追肥用培養液所含之氮量(ppm),ALL係角毛藻於 單位細,耗用之氮量總量(ppm)。CELLAi係補給時間Ai時之 角毛藻早位細胞數,該單位細胞數係由補給時間八丨時之角 毛藻細胞濃度計算之。 上述計算式,亦適用於培養液4、6之單位細胞角毛藻所 耗用之磷總耗用量PALL及矽總耗用量之計算。 圖28係實施例8及9之初期培養液所含氮質量濃度,磷質 量濃度,矽質量濃度,P/N及Si/N。圖28亦表示實施例8之 由角毛藻每1.0X104細胞所耗用之氮總耗用量(ppm),磷總耗 用量(ppm)及矽總耗用量(ppm)計算之磷總耗用量與氮總耗 用I之比(pall/nall)及石夕總耗用量與氮總耗用量之比 (SiALL/NALL)。實施例9亦表示同樣結果。 由上述測定結果獲知; 角毛藻可在約6·〇χ 1〇13細胞/m3附近進行連續而穩定之培 養。 ^ 口 培養液4,6之pH係維持於6.4以上,8.5以下,亦即維持 於7.5以上,8.5以下範圍。NCOMAi, NFIR, NREMAi, NADDAi, NCOMunit, CELLAi and NALL in the above various formulas represent the following amounts, respectively. The amount of nitrogen (ppm) consumed by NCOMAi in the supply time A (il) ~ Ai, NFIR 1294913 is the amount of nitrogen in the initial culture solution (ppm), and the NREMAi is in the replenishment time ^, remaining in the culture The amount of nitrogen in the liquid (ppm), the amount of nitrogen contained in the culture solution for the top dressing when the supply time is μ, and the amount of nitrogen in the fine-grained algae in the unit, the total amount of nitrogen consumed (ppm) . CELLAi is the number of cells in the early stage of the supply of A. cerevisiae. The unit cell number is calculated from the cell concentration of C. albicans at the time of replenishment. The above calculation formula is also applicable to the calculation of the total phosphorus consumption PALL and the total consumption of strontium used by the culture medium 4 and 6. Figure 28 is a graph showing the nitrogen concentration, phosphorus concentration, mass concentration, P/N and Si/N of the initial culture solutions of Examples 8 and 9. Figure 28 also shows the total phosphorus consumption (ppm), total phosphorus consumption (ppm) and total strontium consumption (ppm) of the total amount of phosphorus consumed per 1.0X104 cells of Example 8 in Example 8. The ratio of consumption to total nitrogen consumption (pall/nall) and the ratio of total consumption to total nitrogen consumption (SiALL/NALL). Example 9 also shows the same result. It is known from the above measurement results; Chaetoceros can be continuously and stably cultured at around 6·〇χ 1〇13 cells/m3. ^ The pH of the culture medium 4, 6 is maintained at 6.4 or higher and 8.5 or lower, that is, maintained at 7.5 or higher and 8.5 or lower.
Pall/Nall及Siall/Nall值係接近初期培養液$之p/N及 Si/N值。而pALL/NALL值則接近初期培養液6之p/N值,但 siALL/NALL值則小於初期培養液6之Si/N值。因此,在實驗 皇内之培養瓶11,用培養液4或6培養角毛藻則可於高細胞 ;辰度下連續且穩定培養角毛藻。而培養液4則可於不需添加 -29- 1294913 過剩矽之下,以最佳成分比培養角毛藥。 (實施例10) 對設置於戶外之密閉型反應器,放進含氮(166p㈣,_ - (20 PPm)及矽(60 ppm)之培養液4(65xl(r3 m3),添加碳酸氫 鈉,使碳酸氫納之質量濃度為i.OxiO3 ppm。然後對該培養 液4接種規定量之角毛藻。其次,將培養液溫度維持於約15 °C〜約35°C範圍(宜維持於25。〇,且在照射天然太陽光線(光 量子量:約0〜1200 nm〇l/m2/S之條件下,送進混合3%碳酸氣 之空氣,攪拌培養液4,實施角毛藻培養實驗。分別測定該隹 戶外培養液4之角毛藻細胞濃度之時間變化及pHi時間變 化。 在測定過程中,於角毛藻細胞濃度達約5〇xl〇i3細胞/m3 時’由培養液4取出全量之約一半(33xl〇-3m3)溶液,然後準 備與取出之培養液4同量之溶解SEALIFE而製之人造海 水。對該人造海水溶解含氮、磷、矽及維生素類之追肥成 分則成追肥用培養液。將該追肥用培養液補給於反應器内 之培養液4,實施半批連續培養。 在半批連續培養中,由培養液4取出全量之約一半之溶液 後’分別測定追肥前培養液4a之氮量、磷量及矽量,而計 算该追肥前培養液4a中之氮量、磷量及攻量與初期培養液4 所含之氮量、磷量及^夕量之差距。該初期培養液4之氮量、 磷量及珍量,分別為166 ppm,20 ppm及60 ppm。 根據上述氮量、磷量及矽量之差距,對追肥前培養液4a 補給經調製氮量、磷量及矽量之追肥用培養液,使該追肥 -30- 1294913 初期培養液4之Ρ/Ν(=〇·12)及 可使補給前後之培養液4之Ρ/Ν 用培養液4a之P/Ν及Si/N與 Si/N(-0·36)—致。經此操作 及Si/N —致。 在反覆半批連續培養中,分別測定培養液4之角毛藻細胞 濃度之時間變化及ΡΗ之時間變化,計算單位角毛gixi〇4 細胞 <虱耗用量,磷耗用量及矽耗用量。 圖為實施例1 〇之角毛藥細胞濃度之時間變化圖。圖29 《All係對培養液4首次補給追肥成分之時間。此時,由於 角毛藻細胞濃度尚未達5·0Χ10"細胞/m3,因“從培養液4 抽:約-半溶液。圖29中之A12〜Al7編 胞=達5·〇χ10"細胞/m3以上時,從培養液*抽取全量之約 一 2量又溶液而對培養液4補給追肥用培養液之時間。圖Μ 為實施例1 0之pH之時間變化圖。 實施例1〇,可用與實施例8同樣計算式計算培養液4之时 =細胞(例如紅㈢細胞)中之角毛藥所耗用之氮總耗: ΐ (NALL),磷總耗用量(Pall)及矽總耗用量。 圖31表示實施例10之初期培養液所含氮質量濃度,厂 量濃度’矽質量濃度’ Ρ/Ν及Si/Ne而圖31則表示:據 例10 <每1.〇Χ 1〇4細胞之角毛藻所耗用之氮總耗用= (ppm) ’磷總耗用量(ppm)及石夕總耗用量(ppm)計算之磷細I 用量與氮總耗用量之比(Pall/Nall)及矽總耗用 、耗 用 T 之比(SiALL/NALL)。 耗 由上述測定結果獲知·· 在約5·〇XI〇"細胞/m3附近,可連續且穩定培養角心 ' 毛 果。 -31 - 1294913 培養液4之pH係維持於6.4以上,8.5以下,亦即維持於7.4 以上,8,2以下之範圍内。The Pall/Nall and Siall/Nall values are close to the p/N and Si/N values of the initial culture solution. The pALL/NALL value is close to the p/N value of the initial culture solution 6, but the siALL/NALL value is smaller than the Si/N value of the initial culture solution 6. Therefore, in the culture flask 11 of the experiment, the culture of the cultured liquid 4 or 6 can be used to continuously and stably culture the Chaetoceros under high cell length. The culture solution 4 can be used to culture the horns at the optimum composition ratio without adding -29-1294913. (Example 10) For a closed type reactor installed outdoors, a culture solution 4 (65 x 1 (r3 m3) containing nitrogen (166p (tetra), _ - (20 PPm), and cesium (60 ppm)) was added, and sodium hydrogencarbonate was added. The mass concentration of sodium bicarbonate is i.OxiO3 ppm. Then, the culture solution 4 is inoculated with a predetermined amount of Chaetoceros. Secondly, the temperature of the culture solution is maintained in the range of about 15 ° C to about 35 ° C (should be maintained at 25). 〇, and under irradiation of natural solar light (quantity of light: about 0 to 1200 nm 〇l / m2 / S, the air is mixed with 3% carbonation gas, the culture solution 4 is stirred, and the culture of Chaetoceros is carried out. The time change and pHi time of the C. elegans cell concentration in the outdoor culture solution 4 were measured respectively. During the measurement, the cell concentration of C. cerevisiae was about 5〇xl〇i3 cells/m3, and it was taken out from the culture solution 4. About half (33xl〇-3m3) of the whole amount of the solution, and then prepare the artificial seawater prepared by dissolving SEALIFE in the same amount as the culture solution 4 taken out. The topdressing component containing nitrogen, phosphorus, strontium and vitamins is dissolved in the artificial seawater. The culture solution for top dressing. The culture solution for top dressing is supplied to the culture solution 4 in the reactor. A half batch of continuous culture is carried out. In a half batch of continuous culture, about half of the total amount of the solution is taken out from the culture solution 4, and then the nitrogen amount, the phosphorus amount and the amount of strontium before the pre-dressing culture solution 4a are separately determined, and the pre-fertilization culture solution is calculated. The amount of nitrogen, phosphorus and attack in 4a is different from the amount of nitrogen, phosphorus and amount in the initial culture solution 4. The nitrogen, phosphorus and amount of the initial culture solution 4 are 166 ppm, respectively. 20 ppm and 60 ppm. According to the difference between the amount of nitrogen, the amount of phosphorus and the amount of strontium, the pre-dressing culture solution 4a is supplemented with a dressing culture medium for modulating the amount of nitrogen, phosphorus and strontium, so that the topdressing -30-1294913初期/Ν (=〇·12) of the initial culture solution 4 and Ρ/Ν of the culture solution 4 before and after replenishment. P/Ν and Si/N and Si/N (-0·36) of the culture solution 4a are used. According to this operation and Si/N. In the repeated semi-batch continuous culture, the time change of the concentration of Chaetoceros cells in the culture solution 4 and the time change of the sputum were measured, and the unit gixi〇4 cells were calculated <虱 consumption, phosphorus consumption and consumption consumption. The figure shows the time change of the cell concentration of the horns of the cockroach. Figure 29 The time when the liquid 4 first replenished the top dressing component. At this time, since the cell concentration of the Chaetoceros has not reached 5·0Χ10" cells/m3, because "the pumping solution 4: about-half solution. The A12~Al7 cell in Fig. 29 = up to 5·〇χ10" When the cell/m3 or more, the total amount of the solution is extracted from the culture solution*, and the time for the culture solution 4 is supplemented with the culture solution for the top dressing. Fig. Μ is the time of the pH of the embodiment 10 Variation Example. Example 1 〇, when calculating the culture solution 4 in the same calculation formula as in Example 8, the total nitrogen consumption of the horn horn in the cells (for example, red (three) cells): ΐ (NALL), total phosphorus Consumption (Pall) and total consumption. Fig. 31 is a view showing the mass concentration of nitrogen contained in the initial culture solution of Example 10, the factory concentration '矽 mass concentration' Ρ/Ν and Si/Ne, and Fig. 31 shows: Example 10 <1.〇Χ1〇4 Total nitrogen consumption of C. elegans consumption = (ppm) Ratio of total phosphorus consumption (ppm) and total consumption of phosphorus (ppm) to total phosphorus consumption (Pall/Nall) and the ratio of total consumption and consumption T (SiALL/NALL). It is known from the above measurement results that the cornea can be continuously and stably cultured in the vicinity of about 5·〇XI〇" cells/m3. -31 - 1294913 The pH of the culture solution 4 is maintained at 6.4 or more and 8.5 or less, that is, maintained at 7.4 or more and 8, 2 or less.
Pall/NAll及SIall/Nall則保持接近初期培養液4之P/N及 Si/N數值。因此,在戶外之密閉型反應器放進培養液4培養 角毛藻時,可實施高濃度、連續且穩定之角毛蕩培養。 由上述實施例8〜10之實驗結果可知,培養條件(p/N之 0.12,Si/NSO.3 6),均可適用於室内及室外之連續培養。因 此’相較於先前之培養方法,即使採用連續培養,室内可 在約6.〇xl〇13細胞/m3以上,室外則在約5·〇χΐ〇13細胞/^之 高細胞濃度下,連績且穩定培養角毛藻,至於培養液4之pH 值,不論室内或室外,均維持於6.4以上,8.5以下之範圍内。 而由於角毛藻攝取氮及矽之速度緩慢,於實施例8〜1 〇 中,培養液4,6之初期濃度測定,不一定於角毛藻接種前 貫施’亦可於接種後立即(如圖3 2)或接種後經過半日後實 施。 實施例8〜10係以實際培養角毛藻用之實驗用培養液為對 象,實時測定氮耗用量,磷耗用量及矽耗用量,但亦可以 具有與實驗用培養液同一成分組成之耗用量測定用培養液 為對象,接種角毛藻,預先測定其氮耗用量,磷耗用量及 矽耗用量(參照圖33)。 其依據如下。由本次實驗及分析獲知,單位細胞之角毛 藻之單位時間耗用之氮量(NCOM),磷量(pc〇M)及砍量 (SiCOM) ’在實際培養實驗時之pc〇M/NCOM及SiCOM/ NCOM值係常一定。因此,預先測定耗用量測定用培養液 1294913 中之氮耗用量,磷耗用量及矽耗用量而計算擬培養之矽藻 之PALL/NALL及SiALL/NALL,則可不必於培養實驗之補給時測 定實驗用培養液之氮耗用量,磷耗用量及矽耗用量,根據 預先计算之PALL/NALL及SiALL/NALL,分別調製符合該p/N及 Si/N比之追肥用培養液補給,便可簡化培養工程,且能以 最佳培養液組成實施追肥。 例如,接種於培養液之角毛藻量等於在實施例1〇接種於 培養液4之量時,其PALL/NALL&SiALL/NALL值係分別為〇143 及0.402(參照圖27),因此,將追肥用培養液之 分別設定為0.143及0.402則可。 此外,於實施例8-10,係於角毛藻細胞濃度達約6〇χΐ〇π 細胞/m3以上時,對培養液4補給追肥用培養液,但實際操 作未必如此,該角毛藻細胞濃度得任意設定。 本發明之培養方法之優點如下。 相較於先前之培養方法,本發明之單位容積之角毛藻培 養量增加,因此可降低作業量,培養空間,保管空間及運 輸成本。例如,可減低投入以角毛藻為飼料之水產種苗之 水槽之角毛藻培養液量,由此減少作業量。 於開始培養時可變更角毛藻接種量藉以調整開始培養時 之細胞濃度,由此可預測培養液中之細胞濃度到達所需量 之時間。 上述實施形態係以角毛藻作為接種於培養液之矽藻,但 並不限於此’亦可用其他屬之石夕藻。 例如,分別為三角褐指藻之矽藻(以下稱為三角褐指藻 -33 - 1294913 (Phueodactylum)之培養時係使用具有如圖34之成分組成之 培養液10。培養液10之成分與培養液4相同,而P/N=012, S i/N 0 · 3 6。而培養液11之成分組成係三角褐指、藻培養用之 習知培養液之成分組成。而ρ/Ν=ι·29,Si/N=0(亦即不添加 矽)。 (實施例11) 對實驗室内之扁型培養瓶11(1.5Xl〇-3 m3)放進培養液10 (1·5χ1〇_3 m3),添加碳酸氫鈉,使碳酸氫鈉之質量濃度為 1·〇χ1〇3 ppm。然後對培養液1〇接種規定量之三角褐指藻。 以略同於實施例1之條件(培養液溫度:約25°C〜約35°C,光 量子量:約200 pmol/mVs,以混合3%碳酸氣之空氣通氣攪 拌)培養三角褐指藻,分別測定培養液1 〇之三角褐指藻細胞 濃度之時間變化及pH之時間變化。 (比較例) 對扁培養瓶11放進培養液11(1.5xl0-3 m3),添加碳酸氫 鈉’使碳酸氫鈉之質量濃度為1 ·〇X 1 〇3 ppm。然後對培養液 11接種與實施例11同量之三角褐指藻。以略同於實施例!之 條件(培養液溫度:約25 °C〜約35 °C,光量子量:約200 pmol/m2/s,以混合3%碳酸氣之空氣通氣揽拌),培養三角褐 指藻,分別測定培養液11之三角褐指藻細胞濃度之時間變 化及pH之時間變化。 圖35為實施例11及比較例之三角褐指藻細胞濃度之時間 變化。圖35之Ml,M2表示以培養液10,11培養之三角褐指 藻細胞濃度。 -34- 1294913 圖36為實施例u及比較例之pH之時間變化。圖^之川 N2表示培養液10,^之pH。 由上述測定結果獲知·· 、培養液10之三角褐指漠細㈤濃度可達Μ·2χ1014細胞/m3 以上,而比較例之三角褐指蕩細胞濃度則未達4州〇丨3細胞 /m3 〇 ’ 培養液10之pH係維持於6·4以上,8·5以下範圍 例之pH亦維持於6·4以上,8.5以下範圍Pall/NAll and SIall/Nall maintain the P/N and Si/N values close to the initial culture solution 4. Therefore, when the outdoor closed reactor is placed in the culture solution 4 to culture Chaetoceros, a high concentration, continuous and stable angular hair growth culture can be carried out. From the experimental results of the above Examples 8 to 10, it was found that the culture conditions (0.12 for p/N, Si/NSO.3 6) can be applied to continuous culture indoors and outdoors. Therefore, compared with the previous culture method, even if continuous culture is used, the indoor can be above about 6.〇xl〇13 cells/m3, and the outdoor is at a high cell concentration of about 5·〇χΐ〇13 cells/μ. The pH of the culture solution 4 is maintained at a pH of 6.4 or more and 8.5 or less, both indoors and outdoors. However, since the rate of nitrogen and strontium intake by Char. cerevisiae is slow, in the case of Example 8~1, the initial concentration of the culture solution 4, 6 is not necessarily determined before the inoculation of Chaetoceros', or immediately after inoculation ( See Figure 3 2) or after half a day after inoculation. In the examples 8 to 10, the experimental culture medium for the actual cultivation of Chaetoceros was used to measure the nitrogen consumption, the phosphorus consumption and the consumption amount in real time, but it may also have the same composition as the experimental culture solution. For the consumption of the culture solution for measuring the consumption, the seedlings were inoculated, and the nitrogen consumption, the phosphorus consumption, and the consumption amount were measured in advance (see Fig. 33). Its basis is as follows. According to the experiment and analysis, the amount of nitrogen (NCOM), the amount of phosphorus (pc〇M) and the amount of cut (SiCOM) used per unit time of the unit cell, the pc〇M/ in the actual culture experiment. NCOM and SiCOM/NCOM values are always fixed. Therefore, the PALL/NALL and SiALL/NALL of the algae to be cultured can be calculated by pre-determining the nitrogen consumption, the phosphorus consumption and the consumption of the culture medium 1294913. The nitrogen consumption, the phosphorus consumption and the consumption of the experimental culture solution are measured at the time of replenishment, and the topdressing according to the p/N and Si/N ratios is respectively prepared according to the pre-calculated PALL/NALL and SiALL/NALL. By replenishing with the culture solution, the cultivation process can be simplified, and the top dressing can be carried out with the optimum culture liquid composition. For example, when the amount of Chaetoceros inoculated in the culture solution is equal to the amount inoculated in the culture solution 4 in Example 1, the PALL/NALL&SiALL/NALL values are 〇143 and 0.402, respectively (refer to Fig. 27), and therefore, It is sufficient to set the dressing culture solution to 0.143 and 0.402, respectively. Further, in Example 8-10, when the cell concentration of C. cerevisiae is about 6 〇χΐ〇 π cells/m3 or more, the culture solution 4 is supplemented with the culture solution for top dressing, but the actual operation is not necessarily the case, the C. cerevisiae cell The concentration can be set arbitrarily. The advantages of the culture method of the present invention are as follows. Compared with the prior culture method, the amount of cultured C. elegans per unit volume of the present invention is increased, so that the amount of work, the cultivation space, the storage space, and the transportation cost can be reduced. For example, it is possible to reduce the amount of Chaetoceros culture liquid in the sink of the aquatic seedlings which are fed with the horned algae as a feed, thereby reducing the amount of work. When the culture is started, the amount of the inoculum can be changed to adjust the cell concentration at the start of the culture, thereby predicting the time when the concentration of the cells in the culture solution reaches the desired amount. In the above embodiment, Chaetoceros is used as the algae inoculated in the culture solution, but the present invention is not limited thereto. For example, a culture liquid 10 having a composition as shown in Fig. 34 is used for the culture of the algae of the genus Phaeodactylum (hereinafter referred to as P. euphorbia - 33 - 1294913 (Phueodactylum). The composition and culture of the culture solution 10 The liquid 4 is the same, and P/N = 012, S i / N 0 · 3 6. The composition of the culture solution 11 is composed of a triangular brown finger and a composition of a conventional culture solution for algae culture, and ρ/Ν=ι ·29, Si/N = 0 (ie, no 矽 added). (Example 11) Put the culture flask 10 (1.5×1〇3 m3) in the laboratory into the culture medium 10 (1·5χ1〇_ 3 m3), sodium bicarbonate was added so that the mass concentration of sodium bicarbonate was 1·〇χ1〇3 ppm. Then, the culture solution was inoculated with a predetermined amount of Phaeodactylum tricornutum, which was slightly the same as the condition of Example 1 ( Culture medium temperature: about 25 ° C ~ about 35 ° C, photoquantity: about 200 pmol / mVs, mixed with 3% carbonation gas air aeration and stirring) cultured Trichophytonus tricornutum, respectively, determination of culture medium 1 〇 triangle brown finger Time change of algal cell concentration and time change of pH. (Comparative example) Put the culture medium 11 (1.5xl0-3 m3) into the flat culture flask 11 and add sodium bicarbonate to make sodium bicarbonate The mass concentration was 1 · 〇 X 1 〇 3 ppm. Then, the culture solution 11 was inoculated with the same amount of Phaeodactylum tricornutum as in Example 11. The conditions were similar to those of the examples (culture temperature: about 25 ° C~ Approximately 35 ° C, the quantum of light: about 200 pmol / m2 / s, mixed with 3% carbonation gas air ventilating), cultured Trichophytonus tricornutum, respectively, determine the time change of cell concentration of Phaeodactylum tricornutum And the time change of pH. Fig. 35 shows the time change of the cell concentration of Phaeodactylum tricornutum in Example 11 and Comparative Example. Ml, M2 of Fig. 35 indicates the cell concentration of Phaeodactylum tricornutum cultured in the culture solution 10, 11. - 1294913 Fig. 36 shows the time change of the pH of the examples u and the comparative examples. Fig. 2: Kawagawa N2 indicates the pH of the culture solution 10, and the concentration of the culture medium 10 is determined by the above measurement results. Up to Μ·2χ1014 cells/m3 or more, and the concentration of triangular brown finger cells in the comparative example is less than 4 〇丨3 cells/m3 〇' The pH of the culture solution 10 is maintained above 6.4 or above, below 8·5. The pH of the range is also maintained above 6.4, and below 8.5.
由上述實施例1!之實驗結果可知,使用培養液ι〇培養 角褐指藻時,得以較先前之培養液114高之細胞濃度, 定培養三角褐指藻。 ^卜如同角毛薄’相較於先前之培養方法,可減低作 業量,培養空間,保管空間及輸送成本。 至於在實施例i〜U ’均添加碳酸氫㈣為培養液之邱調 整劑。但是碳酸氫鈉之外,尚可添加含卜之i㈣金屬 (如麵(Li) ’钾(K) ’麵_ ’铯(Cs))等之碳酸氫鹽,以使培 養液内含有碳酸氫鹽。此外,亦可添加2價驗土類金屬作為癱 pH調整劑,使培養液内含碳酸氫鹼金屬鹽之方法。 此外,實施例卜⑴系以混合3%碳酸氣之空氣通氣於培養 液攪拌用’但祇要係維持培養液内生命之成分,亦可使用 添加適宜量之氧氣,二氧化碳等成分之氣體。 此外,本實施形態中,均分別調整培切藻用之培養液 之P/N及㈣,但本發明並不限於該構成,至少對_加以 調整即可。 -35 - 1294913 本發明並未限定於上述實施形態及實施例,祇要不逸出 本發明《王旨’得在適宜範圍内變更實施本發明。 【圖式簡單說明】 圖1係本實施形態所用之培養液之成分。 圖^系由試料之各培養液產生之角毛藻細胞濃度變 化’氮耗用量、磷耗用量及矽耗用量。 圖3 A係氮耗用量與細胞濃度變化之關係。 圖3B係磷耗用量與細胞濃度變化之關係。 圖3C係石夕耗用量與細胞濃度變化之關係。 圖4係本實施形態所用之培養液丨至6之成分組成與先前 培養液7至8之成分組成。 圖5係圖4所示之各培養液所含之氮質量濃度、磷質量濃 度及矽質量濃度。 圖6係培養液4之pH值與水解量之關係。 圖7係本實施形態所用之扁型培養瓶側面圖。 圖8係分別表示對培養液1添加碳酸氫鈉時,及對培養液 不加碳酸氫鈉時之培養液1之pH值與細胞濃度變化之關係。 圖9係將碳酸氫鈉之質量濃度調製為〇 〇2xl〇3 pprn,〇14x 103 ppm及1·〇χ1 〇3 ppm之培養液1之細胞濃度之時間變化。 圖10係將碳酸氫鈉之質量濃度調製為〇.〇2xl〇3 ppm, O·14x 1〇3 PPm及1_〇χίο3 ppm之培養液1之pH值之時間變化。 圖11係將碳酸氫鈉之質量濃度調製為〇.〇7xl〇3 ppm, 〇·14χ 10 Ppm,0·28χ103 ppm及 1.0χ103 ppm之培養液 1 之細 胞濃度之時間變化。 1294913 圖12係將碳酸氫鈉之質量濃度調製為〇 〇7χ1〇3 ρρηι, 0·14χ 103 ppm,0.28xl〇3 ppm及 ΐ·〇χ1〇3 ppm之培養液^阳 值之時間變化。 圖13係將碳酸氫鈉之質量濃度調製為〇·28χ1〇3 pprn, 0·56χ 103ppm,i.〇xi〇3ppm及2 〇xl〇3ppm之培養 之細胞 濃度之時間變化。 圖14係將碳酸氫鈉之質量濃度調製為〇 28χ1〇3 , 0·56χ 103 ppm,ι·〇χ1〇3 ppm及2 〇χ1〇3 之培養液以阳 值之時間變化。 圖15係將碳酸氫鈉之質量濃度調製為1〇χ1〇3 ppm&7 〇x 103 ppm之培養液!之細胞濃度之時間變化。 圖16係將碳酸氫鈉之質量濃度調製為1〇χΐ〇3卯㈤及入⑽ 10 ppm之培養液1之pH值之時間變化。 圖1 7係分別表示實施例丨至4之培養液丨至4之細胞濃度之 時間變化。 圖I8係分別表示實施例丨至4之培養液丨至4之?11值之時間 變化。 固係再見性實驗時之培養液1至4之細胞濃度之時間變 化。 圖20係再現性實驗時之培養液1至4之pH值之時間變化。 圖21係分別表示實施例5至7之培養液2, 4及5之細胞滚度 之時間變化。 圖22係分別表示實施例5至7之培養液2,4及5之阳值之時 1294913 圖23係表示再培養實驗時之培養液2,4及5之細胞濃度之 時間變化。 圖24係表示再培養實驗時之培養液2,4及5之pH值之時間 變化。 圖25係實施例8所用之半批連續培養方法之流程圖。 圖2 6係分別表示實施例8至9之培養液4及6之細胞濃度之 時間變化。 圖27係分別表示實施例8至9之培養液4及6之PH值之時間 變化。 圖28係表示實施例8至9之角毛藻每1.0xlO4細胞之磷總耗 用量與氮總耗用量之比及矽耗用量與氮總耗用量之比。 圖29係實施例1 〇之培養液4之細胞濃度之時間變化。 圖30係實施例1〇之培養液4之pH值之時間變化。 圖3 1係實施例1 〇之角毛藻每1 ·〇χ 1 〇4細胞之磷總耗用量與 氮總耗用量之比及矽總耗用量與氮總耗用量之比。 圖32係半批連續培養法之變形例之流程圖。 圖3 3係半批連續培養法之另一變形例之流程圖。 圖3 4係本實施形態所用之培養液1 〇及π之成分組成。 圖3 5係於實施例11及比較例之培養液1 〇及11之細胞濃度 之時間變化。 圖3 6係於實施例Π及比較例之培養液1 〇及11之pH值之時 間變化。From the experimental results of the above Example 1!, it was found that when the cultured liquid cultivar was cultured with the culture medium, the cell concentration of the culture medium 114 was higher than that of the culture medium 114. ^ Bu, like the corner hair thinner, can reduce the amount of work, the cultivation space, the storage space and the transportation cost compared to the previous culture method. As for the examples i to U', hydrogen carbonate (tetra) was added as a medium conditioner for the culture solution. However, in addition to sodium bicarbonate, bicarbonate such as i (tetra) metal (such as face (Li) 'potassium (K) 'face _ '铯 (Cs)) may be added to make the culture solution contain bicarbonate. . Further, a method of adding a bivalent soil-measuring metal as a hydrazine pH adjusting agent to the alkali metal hydrogencarbonate in the culture solution may be added. Further, in the embodiment (1), the mixture is ventilated with air mixed with 3% carbonic acid gas. However, as long as the component of the life in the culture solution is maintained, a gas containing a suitable amount of oxygen, carbon dioxide or the like may be used. Further, in the present embodiment, P/N and (4) of the culture solution for cultivating algae are separately adjusted. However, the present invention is not limited to this configuration, and at least _ may be adjusted. The present invention is not limited to the above-described embodiments and examples, and the present invention may be modified as appropriate within the scope of the invention. BRIEF DESCRIPTION OF THE DRAWINGS Fig. 1 is a component of a culture solution used in the present embodiment. Fig. 2 shows the change in the concentration of the cells of the Chaetoceros produced by each culture solution of the sample, the amount of nitrogen consumption, the amount of phosphorus consumed, and the amount of consumption. Figure 3 shows the relationship between nitrogen consumption and cell concentration. Figure 3B shows the relationship between phosphorus consumption and cell concentration. Figure 3C shows the relationship between the consumption of Shi Xi and the change of cell concentration. Fig. 4 is a composition of the composition of the culture solution 丨 to 6 used in the present embodiment and the composition of the previous culture liquids 7 to 8. Fig. 5 is a graph showing the nitrogen concentration, the phosphorus mass concentration, and the rhodium mass concentration of each of the culture solutions shown in Fig. 4. Fig. 6 shows the relationship between the pH of the culture solution 4 and the amount of hydrolysis. Fig. 7 is a side view showing a flat type culture bottle used in the embodiment. Fig. 8 is a graph showing the relationship between the pH value of the culture solution 1 and the change in the cell concentration when sodium hydrogencarbonate is added to the culture solution 1, and when the culture solution is not added with sodium hydrogencarbonate. Fig. 9 is a graph showing the time change of the concentration of sodium bicarbonate to the cell concentration of the culture solution 1 of 〇 2xl 〇 3 pprn, 〇 14 x 103 ppm and 1·〇χ1 〇 3 ppm. Figure 10 is a graph showing the time change of the pH of the culture solution 1 of 〇.〇2xl〇3 ppm, O·14x 1〇3 PPm and 1_〇χίο3 ppm. Figure 11 is a graph showing the change in the cell concentration of the sodium bicarbonate to the cell concentration of the culture solution 1 of 〇.〇7xl〇3 ppm, 〇·14χ 10 Ppm, 0·28χ103 ppm and 1.0χ103 ppm. 1294913 Figure 12 is a time-dependent change in the mass concentration of sodium bicarbonate to 培养 〇 7χ1〇3 ρρηι, 0·14χ 103 ppm, 0.28xl〇3 ppm, and ΐ·〇χ1〇3 ppm. Figure 13 is a graph showing the time change of the concentration of sodium bicarbonate to a cell concentration of 培养·28χ1〇3 pprn, 0·56χ 103ppm, i.〇xi〇3ppm and 2〇xl〇3ppm. Fig. 14 is a period in which the mass concentration of sodium hydrogencarbonate is adjusted to 阳 28χ1〇3, 0·56χ 103 ppm, ι·〇χ1〇3 ppm, and 2 〇χ1〇3 of the culture solution at a positive time. Figure 15 is a medium in which the mass concentration of sodium bicarbonate is adjusted to 1〇χ1〇3 ppm&7 〇x 103 ppm! The time of cell concentration changes. Fig. 16 is a graph showing the time change of the pH of the sodium hydrogencarbonate to a pH of 1 〇χΐ〇 3 卯 (5) and (10) 10 ppm of the culture solution 1. Fig. 1 is a graph showing the time change of the cell concentration of the culture solution 丨 to 4 of Examples 丨 to 4, respectively. Figure I8 shows the culture solutions of Examples 丨 to 4, respectively, to 4? The time of the 11 value changes. The time of the cell concentration of the culture solutions 1 to 4 in the solid-state reproducibility experiment was changed. Fig. 20 is a graph showing the time change of the pH of the culture solutions 1 to 4 at the time of the reproducibility experiment. Fig. 21 is a graph showing the time change of the cell rolling degree of the culture solutions 2, 4 and 5 of Examples 5 to 7, respectively. Fig. 22 shows the positive values of the culture solutions 2, 4 and 5 of Examples 5 to 7, respectively. 1294913 Fig. 23 shows the time change of the cell concentration of the culture solutions 2, 4 and 5 at the time of the re-culture experiment. Fig. 24 is a graph showing the time change of the pH values of the culture solutions 2, 4 and 5 at the time of the re-culture experiment. Figure 25 is a flow chart showing the half batch continuous culture method used in Example 8. Fig. 2 is a graph showing temporal changes in cell concentrations of the culture solutions 4 and 6 of Examples 8 to 9, respectively. Fig. 27 is a graph showing the time variation of the pH values of the culture solutions 4 and 6 of Examples 8 to 9, respectively. Figure 28 is a graph showing the ratio of total phosphorus consumption to total nitrogen consumption per 1.0 x 10 O4 cells of Examples 8 to 9 and the ratio of consumption to total nitrogen consumption. Figure 29 is a graph showing the time change of the cell concentration of the culture solution 4 of Example 1. Figure 30 is a graph showing the time change of the pH of the culture solution 4 of Example 1. Fig. 3 1 is the ratio of the total phosphorus consumption to the total nitrogen consumption per 1 · 〇χ 1 〇 4 cells and the ratio of the total strontium consumption to the total nitrogen consumption. Figure 32 is a flow chart showing a modification of the semi-batch continuous culture method. Figure 3 is a flow chart showing another variation of the semi-batch continuous culture method. Fig. 3 is a composition of the composition of the culture solution 1 π and π used in the present embodiment. Fig. 3 is a time change of the cell concentration of the culture solutions 1 and 11 of Example 11 and Comparative Example. Fig. 3 is a time course of pH values of the culture solutions 1 and 11 of the examples and the comparative examples.
Claims (1)
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JP2003338509A JP3990336B2 (en) | 2002-11-28 | 2003-09-29 | Diatom culture method |
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KR (1) | KR100589904B1 (en) |
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CN100400642C (en) * | 2004-06-18 | 2008-07-09 | 徐州师范大学 | Traingular brown algae open culture method and its special culture meidum |
US20090004699A1 (en) * | 2005-10-17 | 2009-01-01 | Yamaha Hatsudoki Kabushiki Kaisha | Process for Producing Beta-Chitin |
WO2007139162A1 (en) * | 2006-05-31 | 2007-12-06 | Incorporated Administrative Agency Fisheries Research Agency | Agent for supplying silicic acid component to algae and method of supplying silicic acid component to algae |
US8437965B2 (en) * | 2010-03-01 | 2013-05-07 | Empire Technology Development Llc | Sensing chemicals in aqueous environments |
CN101984043A (en) * | 2010-11-03 | 2011-03-09 | 王兆凯 | Open cultivation method of diatom |
CN102115714A (en) * | 2010-12-07 | 2011-07-06 | 王兆凯 | Method for performing open cultivation of diatom by adding silicon |
CN103749390B (en) * | 2012-12-24 | 2015-05-13 | 广西壮族自治区海洋研究所 | Method for breeding sipunculus nudus parent |
CN104030451B (en) * | 2014-06-19 | 2016-05-11 | 张家港保税区青山绿水生物科技有限公司 | A kind of method that directive breeding original inhabitants diatom is repaired water body |
CN104170705B (en) * | 2014-08-13 | 2016-03-23 | 盐城工学院 | A kind of beneficial diatoms used for aquiculture cultivates composition |
FR3047998B1 (en) * | 2016-02-24 | 2020-08-28 | Univ Nantes | METHOD OF CULTURE OF PHOTOSYNTHETIC ORGANISMS USING A CO2 SOURCE. |
CN105974055B (en) * | 2016-04-28 | 2018-02-09 | 北京农业信息技术研究中心 | Soilless culture nutrient fluid phosphorus concentration on-line detecting system and detection method |
CN107673874A (en) * | 2017-11-10 | 2018-02-09 | 林东亨 | Diatomeae liquid compound fertilizer and preparation method thereof |
KR101888798B1 (en) | 2017-12-27 | 2018-08-14 | 원종범 | Nano silica solution for culture diatoms and manufacturing method thereof |
KR102152856B1 (en) | 2018-10-29 | 2020-09-07 | 강릉원주대학교산학협력단 | Method of Culturing Freshwater Diatom and Algae for Early Marsh Snail Juveniles |
CN109511580A (en) * | 2018-10-30 | 2019-03-26 | 南宁学院 | A kind of ecological efficient cultural method of mudskipper |
TWI666314B (en) * | 2018-11-15 | 2019-07-21 | National Chung Hsing University | Enhancement of diatom production by using semi-continuous process |
JP7395144B2 (en) * | 2019-04-05 | 2023-12-11 | 三菱重工機械システム株式会社 | Microalgae culture method and microalgae culture device |
NO20201076A1 (en) | 2020-10-01 | 2022-04-04 | Finnfjord As | Process for cultivation of diatoms |
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JPH0965871A (en) * | 1995-09-04 | 1997-03-11 | Kawasaki Steel Corp | Culture of maritime fine algae |
JP2000224981A (en) * | 1999-02-04 | 2000-08-15 | Marine Biotechnol Inst Co Ltd | Medium for marine microalgae and culture of marine microalgae using the same |
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CN100500828C (en) | 2009-06-17 |
KR20040048334A (en) | 2004-06-09 |
CN1504109A (en) | 2004-06-16 |
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