CN2234443Y - Spirulina photosynthesis reactor - Google Patents

Spirulina photosynthesis reactor Download PDF

Info

Publication number
CN2234443Y
CN2234443Y CN95219504U CN95219504U CN2234443Y CN 2234443 Y CN2234443 Y CN 2234443Y CN 95219504 U CN95219504 U CN 95219504U CN 95219504 U CN95219504 U CN 95219504U CN 2234443 Y CN2234443 Y CN 2234443Y
Authority
CN
China
Prior art keywords
column
provided
spirulina
production
pipe
Prior art date
Application number
CN95219504U
Other languages
Chinese (zh)
Other versions
CN2234443K5 (en
Inventor
缪坚人
Original Assignee
缪坚人
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 缪坚人 filed Critical 缪坚人
Priority to CN95219504U priority Critical patent/CN2234443Y/en
Application granted granted Critical
Publication of CN2234443K5 publication Critical patent/CN2234443K5/zh
Publication of CN2234443Y publication Critical patent/CN2234443Y/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
    • C12M41/00Means for regulation, monitoring, measurement or control, e.g. flow regulation
    • C12M41/12Means for regulation, monitoring, measurement or control, e.g. flow regulation of temperature
    • C12M41/18Heat exchange systems, e.g. heat jackets or outer envelopes
    • C12M41/24Heat exchange systems, e.g. heat jackets or outer envelopes inside 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
    • 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
    • C12M23/06Tubular
    • 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
    • C12M23/44Multiple separable units; Modules
    • 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
    • C12M29/02Percolation

Abstract

The utility model relates to a device for microalgae culture and production, particularly a spirulina photosynthesis reactor which is suitable for the photosynthesis reaction of spirulina and algae substance culture and production. The spirulina photosynthesis reactor is composed of a light-permeating reaction tower, and a vertical type double-row flat spiral type pipeline. The top part of the reaction tower is provided with a vent hole; the middle part is provided with a bubbling plate; the lower part is provided with a heat exchanger; the bottom is provided with a CO2 filling pipe. The utility model adopts totally enclosed culture, and is capable of stopping the invasion of any foreign unusual organisms and various chemical pollution factors. The utility model has small ground occupation, energy consumption saving, high biological product rate and all-weather production. The spirulina photosynthesis reactor is suitable for the mass production of high-grade foods and medicine-stage algae products.

Description

螺旋藻光合反应器 Spirulina Photosynthesis Reactor

本实用新型涉及微藻培育生产之装置,特别涉及适用于螺旋藻光合反应与藻生物质的培养生产的装置。 The apparatus of the present invention relates to the production of microalgae cultivation, particularly relates to apparatus suitable for reaction with the culture of photosynthetic algae Spirulina biomass production.

蓝藻螺旋藻(Blue-green Alga,Spirulina Spp.)是一种新颖微生物蛋白质资源。 Spirulina Cyanobacteria (Blue-green Alga, Spirulina Spp.) Is a novel microbial protein resources. 该藻由于含有很高的蛋白质、氨基酸、维生素、不饱和脂肪酸、多糖和矿物质等多种人体需要的营养素,被联合国粮农组织(FAO)、工业发展组织(UNIDO)等推荐为“人类最理想的食品”。 The algae because it contains high protein, amino acids, vitamins, unsaturated fatty acids, polysaccharides and minerals and other nutrients the body needs, the UN Food and Agriculture (FAO), recommended Industrial Development Organization (UNIDO) as the "ideal humanity of food. " 1985年,以本发明人为首的江西省农科院螺旋藻课题研究组,率先建立了我国第一座工厂化大池培养生产系统。 In 1985, the present inventors have led to the Jiangxi Academy of Agricultural Sciences spirulina research group, China's first lead in establishing a factory large pool culture production systems. 此后,类似的装置在全国推广。 Since then, similar devices across the country. 大池培养存在占地面积大、投资成本高、能耗大以及常年生产受气侯影响等问题。 There is a large pool covers an area of ​​cultivation, high investment costs, energy consumption and the production of perennial issue by climate impacts. 近年,CN1098246A推出一种螺旋藻生产方法及装置,它采用沟渠加搅拌方法;另有一种CN2084288U螺旋藻闭式流水线繁育装置,它采用透明塑膜管,在管内通空气的方法。 In recent years, CN1098246A Release spirulina production method and apparatus, which uses trench method plus stirred; spirulina another kind CN2084288U closed breeding line device using a transparent plastic film tube, a method for passing air within the tube. 这些方法与常规大池生产制式相比,前者仍然存在占地面积大,生产受气侯条件影响等问题;后者仍未解决在螺旋藻培养时,由于藻细胞光合产氧发生的蓄积氧中毒问题,以及管道在夏季高温时散热困难及冬季保温困难等技术问题。 These methods of production compared with a conventional large cell format, there is still a large area of ​​the former, affected by weather conditions and other production problems; when the latter is not resolved Spirulina culture, oxygen toxicity problems since the accumulation of the photosynthetic algal cell yield of oxygen generation, and in the summer heat pipe cooling difficulties and difficult winter insulation and other technical issues. 以上制式还由于管道呈平面铺设,只有上层单面可受光,因此仍存在受光面积小,光能利用率不高等问题。 Also since the above standard planar laying pipe, and only the upper single-sided light, so there is still little light receiving area, energy efficiency not high.

本实用新型的目的,在于克服已有螺旋藻生产技术制式中存在的上述问题,设计出一种占地面积很小,能控制温度和光照,可全天侯生产,能进行高效率光合作用,能及时供给并充分利用二氧化碳,能及时排出光合反应过程中产生的氧气的光合反应器。 The purpose of the present invention, to overcome the above problems of the prior art standard spirulina present production, to design a small footprint, can control the temperature and light, can produce all-day, can be performed with high efficiency of photosynthesis, timely and adequate supply of carbon dioxide, the reactor can be discharged in time photosynthetic oxygen produced during the photosynthetic reaction. 以该反应器多单元组合,可进行大生物量连续生产,尤其适用于生产高品位食品、医药级螺旋藻的工业化装置。 In this multi-unit reactor combination, may be continuous production of a large biomass, especially for the production of high-grade food, pharmaceutical grade industrial apparatus Spirulina.

本实用新型的目的采用如下设计实施:本实用新型的光合反应器由光合反应塔与立体双排平螺旋式管道构成。 The object of the present invention using the embodiment designed as follows: The reaction of the present invention is constituted by the photosynthetic photosynthetic reaction tower with a flat double spiral pipe perspective. 该反应器的塔身与管道由高度透光材料构成。 The reactor is composed of a tower with a height of a light-transmitting material conduit. 在塔身顶部设有排气孔用以排除氧气,出液管上端由塔上部引入反应管道,出液管下端置于塔的中下部,进液管从塔的上部引入塔中,塔中部设鼓泡板,在塔下部设热交换器,在塔底部设有CO2注气管,本设计采取立体双排平螺旋式封闭循环管道,配有抽吸泵,出液阀及排液口。 Exhaust hole is provided in the lower part for exclusion of oxygen, the upper end of the tube into the upper portion of the column liquid reaction tubes, the lower end of the liquid pipe is placed at the tower top of the column, inlet tube introduced into the column, the middle column is provided from the upper portion of the column bubbled plate heat exchanger disposed at the bottom of the tower, with CO2 injection tube at the bottom of the column, this design perspective to take a flat spiral double closed-loop pipe, with a suction pump, a liquid valve and the discharge port.

本实用新型的效果显著,它克服了常规大池生产制式占地面积大,能耗大,产率低,且不能金天候生产的弊端。 The utility model is a significant effect, it overcomes the conventional large pool covers an area of ​​large format production, energy consumption, low yield, and can not weather the drawbacks gold production. 它能全方位利用自然光提供光合反应所需的光能、充分满足藻细胞对CO2的需要,并能及时排出有害的培养液中的溶解氧,还由于设有冷/热交换器控制温度,故生产效率高,该反应器由于是全封闭式循环连续生产培养,可以杜绝一切外界异生物和各种化学污染因子的侵染。 It full use of natural light to provide the desired photosynthetic light reaction, algal cells fully meet the needs of CO2, and timely discharged harmful dissolved oxygen in the culture medium, but also because with cold / heat exchanger temperature control, so high production efficiency, since the reactor is a full closed loop continuous production culture, the infection can eliminate all external contamination of various chemical and biological different factors. 故卫生条件好,特别适用于生产高品位食品、医药级产品。 Therefore, health conditions, especially for the production of high-grade food, pharmaceutical grade products.

图面说明:图1.本实用新型光合反应器示意图。 Drawing Description: 1. The present invention is a schematic view of photosynthetic reactor.

下面结合附图与实施例进一步说明本实用新型。 Further embodiments of the drawings below in conjunction with the present invention.

实施例1. Example 1.

1、排气孔 2、出液管3、进液管 4、塔5、鼓泡板 6、进气口7、冷/热水出口 8、热交换器9、冷/热水进口 10、CO2注气管 1, 2 vent, the liquid outlet pipe 3, the inlet tube 4, column 5, bubbling plate 6, intake port 7, cold / hot water outlet 8, the heat exchanger 9, the cold / hot water inlet 10, CO2 Note trachea

11、抽液阀 12、抽吸泵13、排液口 14、出液阀15、平螺旋式管道由图可见,该反应器由反应塔与双排平螺旋式反应管道构成(图中省略管道的中间部份)。 11, the liquid suction valve 12, suction pump 13, the discharge port 14, the liquid valve 15, the flat spiral pipe can be seen, the reactor configuration (omitted from the reaction column and the conduit flat double spiral reaction tubes the middle part). 反应器塔身及管道由高透光率材料构成。 Tower reactor and piping is made of material with high transmittance. 在塔4的顶部设有排气孔,用以排除光合反应中所产生的氧,出液管2上端从塔上部引入反应管道,下端置于塔中下部,进液管3在塔4的上部引入塔中,塔4中间部设有鼓泡板5,在塔4下部设有热交换器8,在塔底部设有CO2注气管10,立体双排平螺旋式封闭管道15上下端与反应塔相连,在螺旋管道15的最底部管道上设有排液口13、抽液阀11及抽吸泵12。 At the top of the column 4 is provided with vent holes for exclusion of oxygen generated in the photosynthesis reaction, the upper end of the liquid pipe 2 is introduced from the upper portion of the column reactor conduit, the lower end of the column is placed in the lower part, the inlet pipe 3 at the upper portion of column 4 introduced into the column, the column 4 is provided with an intermediate portion bubbled plate 5, a heat exchanger 4 in the lower part of the column 8, provided with CO2 gas injection tube 10, the upper and lower ends 15 a perspective double flat spiral duct closed at the bottom of the column and the reaction column connected to the discharge port is provided on the bottommost pipe 15 of helical piping 13, valve 11 and pumping fluid suction pump 12.

本实用新型光合反应器的运行过程如下:在立式双排平螺旋式管道15中积极进行光合反应的培养藻与藻液,流经底部抽液阀11,进入抽吸泵12,通过进液管3,抽至反应塔4的上部,淋注而下。 During operation of the present invention photosynthetic reactor as follows: active flat double spiral in the vertical conduit algae and algae culture solution 15, the bottom of the pumping fluid flowing through the valve 11 of the photosynthetic reaction, into the suction pump 12, through the inlet 3 pipe, pumped to the top of the reactor column 4, and note down leaching. 螺旋藻藻液在塔4中部,受到由进气孔6进入的气体(通过鼓泡板5向上喷气搅动),迅速排除培养液中的氧气。 Spirulina was in the middle of the column 4, by entering from the intake port 6, gas (jet agitation by bubbling up plate 5), was quickly exclude oxygen cultures. 反应塔4同时还继续提供藻生长繁殖所需的光能及由CO2注气管10进入的大量CO2气,使光合反应活跃进行。 Reaction tower 4 while continuing to provide growth and reproduction of algae required by the energy and CO2 injection into the trachea 10 large amount of CO2 gas, the photosynthetic reaction be active. 夏季,在光合反应器中蓄积的大量热量,通过热交换器8的吸热(由下部进水管9送进冷水)后,从上部出水口流出。 After the summer, accumulated in photosynthetic reactor a lot of heat, the endothermic heat exchanger 8 (fed by the lower cold water inlet pipe 9), flows out from the upper outlet. 光合反应器中的培养液经过出液管2,排液阀14进入到平螺旋式管道15中。 Photosynthetic culture liquid in the reactor 2 through the outlet pipe, the drain valve 14 into the conduit 15 in a flat spiral. 在管道15内,螺旋藻活跃进行生长繁殖,细胞大量增殖和产生大量氧气,培养液从双排平螺旋式管道15的上口流向底层管,然后经抽吸泵再次流入反应塔,周而复始循环。 In the pipe 15, spirulina reproduction actively grown, the cells proliferate and produce large amount of oxygen, the culture solution flows from the bottom of the tube catchy flat double spiral pipe 15, and then again into the reaction column via the suction pump, a cycle of. 当培养藻达到一定光密度时,可从底层管排液口13排出采收。 When the algal culture reaches a certain optical density, may be recovered from the bottom of the discharge pipe discharge port 13.

Claims (3)

1.一种螺旋藻光合反应器,由反应塔(4)管道(15)和抽吸泵(12)构成,其特征是:在塔(4)的顶部设有排气孔,出液管(2)上端从塔上部引入反应管道,下端置于塔中下部,进液管(3)在塔(4)的上部引入塔中,塔(4)的中间部设有鼓泡板(5),在塔(4)下部设有冷/热交换器(8),在塔底部设有CO2注气管(10),塔身与立式管道(15)相连,管道(15)的最底部管道上设有排液口(13)、抽液阀(11)和抽吸泵(12)。 A spirulina photosynthetic reactor consists of the reaction column (4) pipes (15) and a suction pump (12), characterized in that: the vent is provided at the top of the column (4), the liquid outlet pipe ( 2) introduced into the reaction pipe from the upper end of the upper portion of the column, the column was placed in the lower end of the lower portion, the inlet pipe (3) into the column at an upper column (4), the column (4) is provided with an intermediate portion bubbled plate (5), in column (4) is provided with a lower cold / heat exchanger (8), provided with CO2 gas injection tube (10) at the bottom of the column (15) is connected to the riser tower, provided on the conduit (15) of the bottommost duct there the discharge port (13), pumping liquid valve (11) and a suction pump (12).
2.根据权利要求1所述的光合反应器,其特征在于:管道(15)采用立体双排平螺旋式封闭结构。 The photosynthetic reactor according to claim 1, wherein: the pipe (15) using three-dimensional flat double spiral closed structure.
3.根据权利要求1、2所述的光合反应器,其特征在于:塔身(4)及双排平螺旋式管道(15)由透光材料构成。 The photosynthetic reactor according to claim 1, wherein: the tower (4) and the flat spiral double pipe (15) made of a translucent material.
CN95219504U 1995-07-31 1995-07-31 Spirulina photosynthesis reactor CN2234443Y (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN95219504U CN2234443Y (en) 1995-07-31 1995-07-31 Spirulina photosynthesis reactor

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN95219504U CN2234443Y (en) 1995-07-31 1995-07-31 Spirulina photosynthesis reactor

Publications (2)

Publication Number Publication Date
CN2234443K5 CN2234443K5 (en) 1996-09-04
CN2234443Y true CN2234443Y (en) 1996-09-04

Family

ID=33867694

Family Applications (1)

Application Number Title Priority Date Filing Date
CN95219504U CN2234443Y (en) 1995-07-31 1995-07-31 Spirulina photosynthesis reactor

Country Status (1)

Country Link
CN (1) CN2234443Y (en)

Cited By (15)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN1066771C (en) * 1996-06-18 2001-06-06 廖明一 Method and apparatus for culturing attached cells
CN1317379C (en) * 2004-07-16 2007-05-23 中国科学院海洋研究所 Pipeline photobioreactor for scale culture of microalgae
JP2007319039A (en) * 2006-05-30 2007-12-13 Chao Hui Lu Photosynthetic reaction system of alga microorganism
CN100404661C (en) * 2004-10-11 2008-07-23 卢朝辉 Vegetal alga, and system and method of microbe potosynthesis reaction
CN101914431A (en) * 2010-07-23 2010-12-15 江苏省海洋水产研究所 Device and method for cultivating microalgae by utilizing all plastic modular photobioreactor system
CN102181366A (en) * 2011-02-23 2011-09-14 叶乃强 Method and device for producing fuel algae in continuous U-shaped tube and application thereof
US20120021496A1 (en) * 2010-07-23 2012-01-26 Eulgi University Industry Academy Cooperation Foundation Method for circulatory cultivating photosynthetic microalgae
EP2412793A1 (en) * 2010-07-30 2012-02-01 Kairos Global Co., Ltd. Circulatory photobioreactor
CN102344888A (en) * 2010-07-29 2012-02-08 凯洛斯环球有限公司 Circulating type photobioreactor
CN102533541A (en) * 2010-12-20 2012-07-04 新奥科技发展有限公司 Microorganism culture system
CN103493732A (en) * 2013-09-18 2014-01-08 天津海友佳音生物科技股份有限公司 Temperature-controllable large-size alga suspension culture device with spore adhesion components
US8658421B2 (en) 2010-07-23 2014-02-25 Kairos Global Co., Ltd. Circulatory photobioreactor
CN102124093B (en) * 2008-06-20 2015-09-02 生物燃料系统有限公司 For by CO 2be converted into the continuous system of high added value and/or nutritive value product and the energy
CN105647826A (en) * 2015-11-11 2016-06-08 深圳市绿得宝保健食品有限公司 Culture method and device of photosynthetic microorganism
CN106635768A (en) * 2015-12-31 2017-05-10 上海绿鼎生物科技有限公司 Biological microalgae photosynthesis reactor and application method thereof

Cited By (21)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN1066771C (en) * 1996-06-18 2001-06-06 廖明一 Method and apparatus for culturing attached cells
CN1317379C (en) * 2004-07-16 2007-05-23 中国科学院海洋研究所 Pipeline photobioreactor for scale culture of microalgae
CN100404661C (en) * 2004-10-11 2008-07-23 卢朝辉 Vegetal alga, and system and method of microbe potosynthesis reaction
JP2007319039A (en) * 2006-05-30 2007-12-13 Chao Hui Lu Photosynthetic reaction system of alga microorganism
CN102124093B (en) * 2008-06-20 2015-09-02 生物燃料系统有限公司 For by CO 2be converted into the continuous system of high added value and/or nutritive value product and the energy
CN101914431A (en) * 2010-07-23 2010-12-15 江苏省海洋水产研究所 Device and method for cultivating microalgae by utilizing all plastic modular photobioreactor system
US20120021496A1 (en) * 2010-07-23 2012-01-26 Eulgi University Industry Academy Cooperation Foundation Method for circulatory cultivating photosynthetic microalgae
US8658421B2 (en) 2010-07-23 2014-02-25 Kairos Global Co., Ltd. Circulatory photobioreactor
CN101914431B (en) * 2010-07-23 2013-05-08 江苏省海洋水产研究所 Device and method for cultivating microalgae by utilizing all plastic modular photobioreactor system
CN102344888A (en) * 2010-07-29 2012-02-08 凯洛斯环球有限公司 Circulating type photobioreactor
CN102344888B (en) * 2010-07-29 2014-08-20 凯洛斯环球有限公司 Circulating type photobioreactor
EP2412793A1 (en) * 2010-07-30 2012-02-01 Kairos Global Co., Ltd. Circulatory photobioreactor
CN102533541A (en) * 2010-12-20 2012-07-04 新奥科技发展有限公司 Microorganism culture system
CN102533541B (en) * 2010-12-20 2015-04-15 新奥科技发展有限公司 Microorganism culture system
CN102181366A (en) * 2011-02-23 2011-09-14 叶乃强 Method and device for producing fuel algae in continuous U-shaped tube and application thereof
CN103493732A (en) * 2013-09-18 2014-01-08 天津海友佳音生物科技股份有限公司 Temperature-controllable large-size alga suspension culture device with spore adhesion components
CN103493732B (en) * 2013-09-18 2016-05-18 天津海友佳音生物科技股份有限公司 A kind of controllable temperature macro suspension culture apparatus with Spore adhesion parts
CN105647826A (en) * 2015-11-11 2016-06-08 深圳市绿得宝保健食品有限公司 Culture method and device of photosynthetic microorganism
CN105647826B (en) * 2015-11-11 2019-05-10 深圳市绿得宝保健食品有限公司 A kind of cultural method and device of photosynthetic microorganism
CN106635768A (en) * 2015-12-31 2017-05-10 上海绿鼎生物科技有限公司 Biological microalgae photosynthesis reactor and application method thereof
CN106635768B (en) * 2015-12-31 2019-07-23 上海绿鼎生物科技有限公司 Biological microalgae photosynthetic reactor and its application method

Also Published As

Publication number Publication date
CN2234443K5 (en) 1996-09-04

Similar Documents

Publication Publication Date Title
US8722396B2 (en) Bioreactor assembly for culture of photoautotrophic algae
JP2698308B2 (en) Microbial growth apparatus
US8586353B2 (en) Closed photobioreactor system for continued daily In Situ production of ethanol from genetically enhanced photosynthetic organisms with means for separation and removal of ethanol
Watanabe et al. Photosynthetic performance of a helical tubular photobioreactor incorporating the cyanobacterium Spirulina platensis
US8877486B2 (en) Photobioreactor for carbon dioxide mitigation in wastewater treatment
US20130109008A1 (en) Method and apparatus for growing photosynthetic organisms
AU2004256839B2 (en) Multi-layered photobioreactor and method of culturing photosynthetic microorganisms using the same
Pulz et al. Photobioreactors: design and performance with respect to light energy input
US8658420B2 (en) Photobioreactor for algae growth
US20110070632A1 (en) Photo bioreactor and cultivation system for improved productivity of photoautotrophic cell cultures
JP4405980B2 (en) Plant algae / microorganism photosynthesis reactor
CN104030518B (en) A kind of ultra-large light of Water warfare catches bio-reactor and operation method
JP3111873U6 (en) Plant algae / microorganism photosynthesis reactor
US7851211B2 (en) Alga microbe photosynthetic reaction system
CN101870950B (en) Device for culturing microalgae
CN103865793B (en) Nostoc algae shallow-layer culture systems and cultural method
Lee Enclosed bioreactors for the mass cultivation of photosynthetic microorganisms: the future trend
CN101050419B (en) Production apparatus for culturing tiny alga and production method
EP1599570A2 (en) Reactor for industrial culture of photosynthetic micro-organisms
CN100587054C (en) Novel multi-section flat type photo-bioreactor
CN102618434B (en) High-efficiency microalgae culturing device based on plant bionics
CN1314795C (en) Pneumatically liftable photo-biologic reactor for high density culture of algae
CN101914431B (en) Device and method for cultivating microalgae by utilizing all plastic modular photobioreactor system
US7056725B1 (en) Vegetable alga and microbe photosynthetic reaction system and method for the same
CN101280271A (en) Production unit for microalgae industrialization and method for producing microalgae

Legal Events

Date Code Title Description
C14 Grant of patent or utility model
C19 Lapse of patent right due to non-payment of the annual fee