TWI299652B - Algae Culture System - Google Patents

Algae Culture System Download PDF

Info

Publication number
TWI299652B
TWI299652B TW94144141A TW94144141A TWI299652B TW I299652 B TWI299652 B TW I299652B TW 94144141 A TW94144141 A TW 94144141A TW 94144141 A TW94144141 A TW 94144141A TW I299652 B TWI299652 B TW I299652B
Authority
TW
Taiwan
Prior art keywords
culture
algae
cultivation system
liquid
culture tank
Prior art date
Application number
TW94144141A
Other languages
Chinese (zh)
Other versions
TW200721968A (en
Inventor
Wen Chang Lu
Shu-Mei Yang
Original Assignee
Ind Tech Res Inst
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Ind Tech Res Inst filed Critical Ind Tech Res Inst
Priority to TW94144141A priority Critical patent/TWI299652B/en
Priority to JP2006334638A priority patent/JP4588692B2/en
Publication of TW200721968A publication Critical patent/TW200721968A/en
Application granted granted Critical
Publication of TWI299652B publication Critical patent/TWI299652B/en

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C12BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
    • C12MAPPARATUS FOR ENZYMOLOGY OR MICROBIOLOGY; APPARATUS FOR CULTURING MICROORGANISMS FOR PRODUCING BIOMASS, FOR GROWING CELLS OR FOR OBTAINING FERMENTATION OR METABOLIC PRODUCTS, i.e. BIOREACTORS OR FERMENTERS
    • C12M21/00Bioreactors or fermenters specially adapted for specific uses
    • C12M21/02Photobioreactors
    • CCHEMISTRY; METALLURGY
    • C12BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
    • C12MAPPARATUS FOR ENZYMOLOGY OR MICROBIOLOGY; APPARATUS FOR CULTURING MICROORGANISMS FOR PRODUCING BIOMASS, FOR GROWING CELLS OR FOR OBTAINING FERMENTATION OR METABOLIC PRODUCTS, i.e. BIOREACTORS OR FERMENTERS
    • C12M23/00Constructional details, e.g. recesses, hinges
    • C12M23/02Form or structure of the vessel
    • CCHEMISTRY; METALLURGY
    • C12BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
    • C12MAPPARATUS FOR ENZYMOLOGY OR MICROBIOLOGY; APPARATUS FOR CULTURING MICROORGANISMS FOR PRODUCING BIOMASS, FOR GROWING CELLS OR FOR OBTAINING FERMENTATION OR METABOLIC PRODUCTS, i.e. BIOREACTORS OR FERMENTERS
    • C12M29/00Means for introduction, extraction or recirculation of materials, e.g. pumps
    • C12M29/06Nozzles; Sprayers; Spargers; Diffusers
    • CCHEMISTRY; METALLURGY
    • C12BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
    • C12MAPPARATUS FOR ENZYMOLOGY OR MICROBIOLOGY; APPARATUS FOR CULTURING MICROORGANISMS FOR PRODUCING BIOMASS, FOR GROWING CELLS OR FOR OBTAINING FERMENTATION OR METABOLIC PRODUCTS, i.e. BIOREACTORS OR FERMENTERS
    • C12M29/00Means for introduction, extraction or recirculation of materials, e.g. pumps
    • C12M29/18External loop; Means for reintroduction of fermented biomass or liquid percolate

Landscapes

  • Health & Medical Sciences (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Organic Chemistry (AREA)
  • Chemical & Material Sciences (AREA)
  • Bioinformatics & Cheminformatics (AREA)
  • Wood Science & Technology (AREA)
  • Zoology (AREA)
  • Biotechnology (AREA)
  • Genetics & Genomics (AREA)
  • General Engineering & Computer Science (AREA)
  • Biochemistry (AREA)
  • Biomedical Technology (AREA)
  • General Health & Medical Sciences (AREA)
  • Sustainable Development (AREA)
  • Microbiology (AREA)
  • Molecular Biology (AREA)
  • Clinical Laboratory Science (AREA)
  • Apparatus Associated With Microorganisms And Enzymes (AREA)
  • Cultivation Of Seaweed (AREA)

Description

1299652 九、發明說明: 【發明所屬之技術領域】 本發明是關於一種培養系統,特別是關於一種藻類培養 系統。 【先前技術】1299652 IX. DESCRIPTION OF THE INVENTION: TECHNICAL FIELD The present invention relates to a culture system, and more particularly to an algae cultivation system. [Prior Art]

▲、由於化石燃料面臨枯竭危機,如何藉由生物技術來產生 旎源以作為新的替代性能源,也成為非常重要的議題。以生物 技術可產製的生物燃料種類相當多,例如經由厭氧醱酵程序生 ,甲,或氫,、微藻類培養生產氫氣(藍綠藻類)或生質柴油 (矽深、綠澡類)等。自1980年起,就開始研究以生質柴油 ΐί來替代柴油燃料;於1930到_年間,則利用蔬菜油作 二木油燃料’生質柴油燃料相較於柴油燃料主要的優點則是且 有低濃度的溫室效應氣體(特別是二氧化碳)及污染物。八 菩丰ίίΓΠ)與太陽能研究學會於1979年也開始 究,發現相較於其他植物,藻類儲 2豆此被視為有潛力生物原料,可用來轉化成辦 例如和&油㈣。鶴所含有的脂肪和油的含量 1似於蔬菜油,然而任何—可獲得2(Mg _的 均油脂含量,有些_甚至可獲得8() wt%的人旦。缺 相較於藉由藻類_而產生曱烧或乙醇 j 的方法因==: 二c i心里油月日滞種,將澡種的油脂轉化成生質柴油, 不僅可做騎代麟更可增加經濟附加價值 ^ 油脂的產量,作為生質柴油的料源,戶:J y曰加_ 養殖系統是必須的,所以開發新型高效。二 糸統’改善傳統的藻類培養系統,成為發展替以:i: • 1299652 課題之一。 、,於澡類是自營性生物,二氧化碳為辅助生長的竣源, ^以《5有效率的培養系統,其藻類利用二氧化碳的效率也越 同三澡類培養系統大致可分為開放系統與密閉系統兩種,習知 的藻類開放式培養系統主要有圓形培養池(Circular卿幻及 跑道式培養池(Race-way pond)兩種,圓形培養池早期曾盛行 f内’而’其具有攪拌不均勻、_耗能高、ΐ體 rri”地糊不充分等缺點,目前只於少數地方仍有使 ϊΐϊΓΓ。雖然跑道式培養池已改 ㈣田」勾及耗相通,然而,仍存在氣體混合不均及 效率不佳需廣大培養土地等問題。因此, 用效率佳、溫度及濃度容易㈣、侧在 及規模放大料之培養祕。 你规應力低以 【發明内容】 本發明的主要目的在於提供—種藻類终 統設計解決藻類養殖問題,增加藻類培養面^養…猎由糸 環裴置。底 養 動,其包含有底部盛液培養槽、# ^ : 部盛液培娜置有培養藻液,培裝置。 槽的·^方。紐循職置係抽取底 並持續地將培養藻液通人培養|置,使培^裝^內^養澡, 溢流至底部盛液培養槽。藉由培養培養漆液 培養槽之_環,可增加_培#光昭面f H與底部盛液 培養時間,並提高產量。長桃分佈不__題,縮短 本發明實關之培魏置包含有至少—培養池。 • 1299652 抵芦士發明實施例包含氣體源,用以提供培養氣體,且μ 含氣齡配裝置,氣齡配裝置連接 二 ,,體通人培養藻液,增加培養溶液中培養氣心 如幵軋體流動路徑及增加反應容積。 、/辰又並 發明實施例的底部盛液培養槽之底部中心為最板點, =體俩裝置可連接於最低點,培養藻液中的 點’可經由流體循環裝i送入轉震 至、、盾二至取低 面積的目的。 财置u_增加藻類培養 了解 兹詳細為ίΐ本下㈣的目的、槪及其舰有進-步的 【實施方式】 本發明實施例所揭露之藻類谇表♦ ^ 液循環流動,請參考第丨圖,复為Υ、、、、,、以使培養澡 包含有底部盛躲4 轉圖。其 及氣體源14G。底部盛液培養槽^ 環裝置13〇 養裝置120設置於底部盛液培養槽11{)^^養=⑵,培 13〇係抽取底部盛液培養槽110 的亡方。机體循環裝置 液121溢流至底部盛液培養槽11〇。k養裝i 120⑽培養藻 如弟1圖所示,培養裳詈】 一 底部盛液培顧110上方堆~_ =有三個轉池,係於 121,且由上方溢流而下的么35養池溢流之培養薄液 下層之擾動,將使培H^ j121卿重力財式造成 均勾。如此,可增加的藻體懸浮流動進而混合 其中,培養池係為環狀,故流體循環裝請^穿各 J299652 培養池抽取底部盛液培養槽110的培養藻液121,再持續 地將培養藻液121通入最頂端之培養池,上方培養池培養藻液 則溢流至下方的培養池,最後流人底部盛液培養槽。 循環裝置130更包含氣體分配裝置131,氣體分配裝置 接至氣體源14G,以將培養紐通人培養絲121,增加 ί液ϋ Γ轉紐,並提昇氣财祕徑及增加^容 培養槽110設計成㈣,使底部中心為最低點, G連接於最低點,使藻體不致累積沉降,, 由流體循環裝置130送入培養裝置12〇。 巧J心▲Because of the depletion crisis of fossil fuels, how to use biotechnology as a new alternative energy source has become a very important issue. There are quite a variety of biofuels that can be produced by biotechnology, such as anaerobic fermentation, A, or hydrogen, and microalgae culture to produce hydrogen (blue-green algae) or biodiesel (deep, green bath). Wait. Since 1980, it has been researched to replace diesel fuel with biodiesel. In 1930 to _ years, vegetable oil was used as a fuel for two wood oils. The main advantages of biodiesel fuel compared to diesel fuel are Low concentrations of greenhouse gases (especially carbon dioxide) and pollutants. Eight Bodhi ίίΓΠ) and the Solar Energy Research Society also began research in 1979 and found that compared to other plants, algae storage 2 beans are considered as potential biological raw materials, which can be used to convert into, for example, & oils (4). The content of fat and oil contained in the crane is similar to that of vegetable oil. However, any can obtain 2 (Mg _ of the average oil content, some _ even get 8 () wt% of the human den. The lack of phase compared to algae _ The method of producing simmering or ethanol j ===: The second ci heart oil is stagnation, and the oil of the bath is converted into biodiesel, which can not only increase the economic added value of the dynasty. As a source of biodiesel, households: J y曰 加 _ farming system is a must, so the development of new high-efficiency. Dioxi 'improving the traditional algae cultivation system, becoming a development alternative: i: • 1299652 In the bath, it is a self-supporting organism, and carbon dioxide is a source of auxiliary growth. ^With the 5 efficient culture system, the efficiency of algae using carbon dioxide is also roughly the same as that of the three-bath culture system. There are two kinds of open algae open culture systems, which are mainly circular circular culture ponds (Circular Qingyue and Race-way pond). The circular culture ponds have been popular in the early days. It has uneven mixing, high energy consumption, and ΐ The shortcomings of the body rri are not sufficient. At present, there are still a few sputum in a few places. Although the runway culture tank has been changed (four) field and the consumption is the same, however, there are still uneven gas mixing and poor efficiency. Problems such as land. Therefore, it is easy to use, and the temperature and concentration are easy. (4), side-by-side and scale-up materials are cultivated. The stress is low. [Inventive content] The main purpose of the present invention is to provide an algae-like design to solve algae. Breeding problem, increase the algae culture surface ^ raise... Hunting is set by the 糸 ring. The bottom nutrient, which contains the bottom liquid culture tank, # ^ : The part of the liquid liquid Pei Na has a cultured algae liquid, a culture device. ^方. New Zealand is based on the bottom of the line and continuously cultured the algae liquid through the human culture | set, so that the culture is filled with a bath, overflowing to the bottom liquid culture tank. By cultivating the culture paint tank _ ring, can increase _ Pei #光昭面 f H and the bottom liquid culture time, and increase the yield. Long peach distribution is not __ questions, shorten the practice of the invention, the Wei Wei set contains at least - the culture pool. • 1299652 The invention of the invention includes gas The source is used for supplying a culture gas, and the gas-containing age-matching device is connected to the gas-aged device, and the body-passing human culture liquid is added to increase the culture gas center such as the flow path of the rolling body and increase the reaction volume. / Chen also invented the bottom of the bottom liquid culture tank of the embodiment of the bottom of the bottom plate, the body device can be connected to the lowest point, the point in the cultured algae liquid can be sent to the shock through the fluid circulation Shield 2 to the purpose of taking a low area. The accumulation of u_increased algae cultivation is understood in detail as the purpose of (4), and its ship has advanced. [Embodiment] The algae disclosed in the embodiments of the present invention Table ♦ ^ Liquid circulation flow, please refer to the figure, re-established as Υ, ,,,,, so that the culture bath contains a bottom to avoid 4 turn. It is also a gas source 14G. The bottom liquid culture tank ^ ring device 13 is provided in the bottom liquid culture tank 11 {) ^ ^ ^ = (2), and the bottom of the bottom liquid culture tank 110 is extracted. The body circulation device liquid 121 overflows to the bottom liquid culture tank 11〇. k cultivating i 120 (10) culture algae as shown in the figure 1 of the younger brother, cultivating the scorpion 詈 一 一 一 一 一 一 一 一 一 一 一 110 110 110 110 ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ The disturbance of the lower layer of the thin liquid in the pool overflow will cause the H^j121qing gravity method to cause the hook. In this way, the increased algae suspension flow is further mixed, and the culture tank is ring-shaped, so the fluid circulation device is required to pass through the J299652 culture tank to extract the culture algae liquid 121 of the bottom liquid culture tank 110, and then continuously culture the algae. The liquid 121 is passed into the topmost culture tank, and the culture liquid in the upper culture tank overflows to the lower culture tank, and finally flows into the bottom liquid culture tank. The circulation device 130 further includes a gas distribution device 131, and the gas distribution device is connected to the gas source 14G to culture the Newton human culture wire 121, increase the liquid pressure, and increase the gas path and increase the capacity of the culture tank 110. Designed as (4), the bottom center is the lowest point, G is connected to the lowest point, so that the algae body does not accumulate, and is sent to the culture device 12 by the fluid circulation device 130. Qiao J heart

士拉ff ’培養池之邊緣具有複數健出結構,使培養薄液 Ϊ 能夠均句地流出:以 出結義可為=/= 彡發明實酬之如結構示意圖,突 本發明之較佳實施例揭露如上所述,然其並非用w ^内可藝者’在不麟本^之精神和 圍須视本說轉利保護範 J299652 【圖式簡單說明】 第1圖為本發明實施例之示意圖;及 第2A圖及第2B圖為本發明實施例之突出結構示意圖。 【主要元件符號說明】 110 底部盛液培養槽 120 培養裝置 121 培養藻液 122 突出結構 130 流體循環裝置 131 氣體分配裝置 140 氣體源Syrah ff's edge of the culture tank has a plurality of nutrient structures, so that the culture liquid sputum can flow out uniformly: the clarification can be === 彡 the invention as a structural schematic diagram, the preferred embodiment of the invention is disclosed As described above, it is not a w ^ in the art of the 'in the spirit of the ^ 本 ^ ^ ^ ^ ^ ^ ^ J J J 299 299 299 299 299 299 299 299 299 299 299 299 299 299 299 299 299 299 299 299 299 299 299 299 299 299 299 2A and 2B are schematic views showing the protruding structure of the embodiment of the present invention. [Explanation of main component symbols] 110 Bottom liquid culture tank 120 Culture device 121 Culture algae liquid 122 Projection structure 130 Fluid circulation device 131 Gas distribution device 140 Gas source

Claims (1)

1299652 (97Ο5,27) " --------- 々··月日修(更)正本 十、申請專利範圍: ——一一 一 一一」 L種滅類培養系統,係用以使一培養藻液循環流動,包含·· 一底部盛液培養槽,容置有該培養藻液; 一培養裝置,設置於該底部盛液培養槽的上方; 一流體循環裝置,抽取該底部盛液培養槽的該培養藻液, 並持續地將該培養藻液通入該培養裝置,使該培養裝置内的該 _ 培養藻液溢流至該底部盛液培養槽。 2·如申請專利範圍第1項所述之藻類培養系統,其中該培養裝置包 含有至少一培養池。 3·如申請專利範圍第2項所述之藻類培養系統,其中該培養池之邊 緣具有複數個突出結構。 4·如申明專利範圍第3項所述之藻類培養系統,其中該突出結構為 V形或方形。 • 5·如申請專利範圍第1項所述之藻類培養系統,其中該培養裝置包 含複數培養池’係於遠底部盛液培養槽上方堆疊排列。 .6·如申請專利範圍第5項所述之藻類培養系統,其中該培養裝置包 含之各該培養池由上而下地面積遞增,使下方的該培養池能夠 承接上方該培養池溢流之培養藻液。 7·如申請專利範圍第5項所述之藻類培養系統,其中該流體循環裝 置係將該培養藻液通入培養裂置之底端,再至最頂端之該典養 池。 10 1299652 8. 如申請專利範圍第1項所述之藻類培養系統,更包含一氣體源, 係提供一培養氣體。 9. 如申請專利範圍第1項所述之藻類培養系統,其中該流體循環裝 置包含一氣體分配裝置,係連接至該氣體源,以將該培養氣體 通入該培養藻液。 10. 如申請專利範圍第1項所述之藻類培養系統,其中該底部盛液 培養槽之底部中心為一最低點。 11. 如申請專利範圍第10項所述之藻類培養系統,其中該流體循環 裝置連接於該最低點。 12. 如申請專利範圍第1項所述之藻類培養系統,其中該底部盛液 培養槽為V形。1299652 (97Ο5,27) " --------- 々··月日修 (more) 正本10, the scope of application for patent: ——1111 1" L species of cultivating system, used In order to circulate a cultured algae liquid, comprising: a bottom liquid culture tank containing the culture algae liquid; a culture device disposed above the bottom liquid culture tank; a fluid circulation device extracting the bottom portion The cultured algae solution in the liquid culture tank is continuously passed to the culture apparatus, and the culture liquid in the culture apparatus is overflowed to the bottom liquid culture tank. 2. The algae cultivation system of claim 1, wherein the culture device comprises at least one culture tank. 3. The algae cultivation system of claim 2, wherein the edge of the culture tank has a plurality of protruding structures. 4. The algae cultivation system of claim 3, wherein the protruding structure is V-shaped or square. 5. The algae cultivation system according to claim 1, wherein the culture device comprises a plurality of culture cells stacked on top of the bottom liquid culture tank. 6. The algae cultivation system according to claim 5, wherein the culture device comprises an increase in the area of each of the culture cells from top to bottom, so that the lower culture tank can receive the culture of the above culture tank overflow. Algae solution. 7. The algae cultivation system of claim 5, wherein the fluid circulation device passes the cultured algae liquid to the bottom end of the culture disruption to the topmost pond. 10 1299652 8. The algae cultivation system according to claim 1, further comprising a gas source for providing a culture gas. 9. The algae cultivation system of claim 1, wherein the fluid circulation device comprises a gas distribution device coupled to the gas source to pass the culture gas into the culture algae solution. 10. The algae cultivation system of claim 1, wherein the bottom center of the bottom liquid culture tank is a lowest point. 11. The algae cultivation system of claim 10, wherein the fluid circulation device is coupled to the lowest point. 12. The algae cultivation system of claim 1, wherein the bottom liquid culture tank is V-shaped. 1111
TW94144141A 2005-12-13 2005-12-13 Algae Culture System TWI299652B (en)

Priority Applications (2)

Application Number Priority Date Filing Date Title
TW94144141A TWI299652B (en) 2005-12-13 2005-12-13 Algae Culture System
JP2006334638A JP4588692B2 (en) 2005-12-13 2006-12-12 Algae culture system

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
TW94144141A TWI299652B (en) 2005-12-13 2005-12-13 Algae Culture System

Publications (2)

Publication Number Publication Date
TW200721968A TW200721968A (en) 2007-06-16
TWI299652B true TWI299652B (en) 2008-08-11

Family

ID=38243173

Family Applications (1)

Application Number Title Priority Date Filing Date
TW94144141A TWI299652B (en) 2005-12-13 2005-12-13 Algae Culture System

Country Status (2)

Country Link
JP (1) JP4588692B2 (en)
TW (1) TWI299652B (en)

Families Citing this family (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
ES2341194B1 (en) * 2007-09-11 2011-04-26 Francisco Angulo Lafuente METHOD OF OBTAINING A PARAFFIN, THROUGH A BIOLOGICAL PROCESS WITH MICROORGANISMS, FROM ORGANIC MATERIAL AND ITS REFINING METHOD TO BE USED AS FUEL.
JP5810831B2 (en) * 2011-10-26 2015-11-11 株式会社デンソー Algae culture method
CN102618434B (en) * 2012-02-17 2014-02-19 农业部规划设计研究院 High-efficiency microalgae culturing device based on plant bionics
CN106544266A (en) * 2016-10-08 2017-03-29 东莞市万融生物科技有限公司 Equipment for microalgae cultivation and technological process
CN110317711A (en) * 2019-07-11 2019-10-11 湖北盛齐安生物科技股份有限公司 The equipment induced cell apoptosis and its method for promoting cell to discharge vesica
CN110628578B (en) * 2019-09-30 2024-03-08 旭无线(宁波)智能卫浴有限公司 Microalgae cultivation equipment and use method thereof
JP7462308B2 (en) * 2020-08-11 2024-04-05 株式会社BrainGild Cultivation device and method for producing cultured object
CN113403185A (en) * 2021-06-09 2021-09-17 贵州民族大学 Algae inoculator and inoculation method

Family Cites Families (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5376550A (en) * 1976-12-17 1978-07-07 Sumitomo Chem Co Ltd Method of biologically treating sewage in multistage type
JPS61230786A (en) * 1985-04-05 1986-10-15 Aikurinpia:Kk Biological filter apparatus
JPH02191593A (en) * 1989-01-17 1990-07-27 Japan Vilene Co Ltd Reactor for immobilized physiologically active material
JPH04267997A (en) * 1991-02-25 1992-09-24 Japan Vilene Co Ltd Reaction method of physiologically active substrate
JP3035153B2 (en) * 1994-04-27 2000-04-17 石川島播磨重工業株式会社 Culture method for photosynthetic organisms
JPH08140662A (en) * 1994-11-22 1996-06-04 Mitsui Eng & Shipbuild Co Ltd Culture of fine algae in high concentration by utilization of deep layer water and device therefor
JP2000015276A (en) * 1998-07-02 2000-01-18 Hitoshi Hayakawa Filter apparatus
JP2004000298A (en) * 2003-09-25 2004-01-08 Yanmar Co Ltd Microbial cultivation system

Also Published As

Publication number Publication date
JP4588692B2 (en) 2010-12-01
TW200721968A (en) 2007-06-16
JP2007159582A (en) 2007-06-28

Similar Documents

Publication Publication Date Title
TWI299652B (en) Algae Culture System
Ozkan et al. Reduction of water and energy requirement of algae cultivation using an algae biofilm photobioreactor
Xu et al. Microalgal bioreactors: challenges and opportunities
Pulz et al. Photobioreactors: design and performance with respect to light energy input
Aghaalipour et al. Carbon dioxide capture with microalgae species in continuous gas-supplied closed cultivation systems
CN102206570B (en) Apparatus and cultivating method for scaled cultivation of microalgae
US20100099151A1 (en) Vertical submersible photobioreactor for obtaining biofuels
Öncel et al. Façade integrated photobioreactors for building energy efficiency
WO2011050578A1 (en) Method for culture of microalgae and photobioreactor system thereof
Egbo et al. Photobioreactors for microalgae cultivation–an overview
CN103981083B (en) The closed mixotrophic cultivation method of a kind of micro-algae
WO2019165689A1 (en) Microbubble photobioreactor for economic microalgae cultivation
CN105002086A (en) Runway pool microalgae culture system using micro-bubble continuous gas flotation to harvest algal cells
Yang et al. Experimental study on microalgae cultivation in novel photobioreactor of concentric double tubes with aeration pores along tube length direction
US9206388B1 (en) Process for a sustainable growth of algae in a bioreactor and for the extraction of a biofuel product
CN104328074A (en) Microalgae cultivation method under low illumination condition
May-Cua et al. A cylindrical-conical photobioreactor and a sludge drying bed as an efficient system for cultivation of the green microalgae Coelastrum sp. and dry biomass recovery
Fallahi et al. Effects of simultaneous CO2 addition and biomass recycling on growth characteristics of microalgal mixed culture
Majid et al. Production of algal biomass
CN204874506U (en) Utilize microbubble to last gather little algae farming systems in runway pond of frustule of air supporting
CN206799614U (en) A kind of microalgae culturing device adopting of aerostatic buoyancy and GRAVITY CONTROL loop direction
CN107904158A (en) A kind of film aeration microalgae biological film culture device and operation method
CN106636264A (en) Method for producing phycoerythrin and polyunsaturated fatty acid by using R. salina
TWI479988B (en) Carbon dioxide-capturing apparatus for microalgae cultivation and the method thereof
CN109251847A (en) Utilize the device and method of sunlight culture photosynthetic microorganism