CN2234443Y - Spirulina photosynthesis reactor - Google Patents
Spirulina photosynthesis reactor Download PDFInfo
- 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
- tower
- spirulina
- pipeline
- production
- utility
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Fee Related
Links
Images
Classifications
-
- C—CHEMISTRY; METALLURGY
- C12—BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
- C12M—APPARATUS 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
- C12M41/00—Means for regulation, monitoring, measurement or control, e.g. flow regulation
- C12M41/12—Means for regulation, monitoring, measurement or control, e.g. flow regulation of temperature
- C12M41/18—Heat exchange systems, e.g. heat jackets or outer envelopes
- C12M41/24—Heat exchange systems, e.g. heat jackets or outer envelopes inside the vessel
-
- C—CHEMISTRY; METALLURGY
- C12—BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
- C12M—APPARATUS 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
- C12M21/00—Bioreactors or fermenters specially adapted for specific uses
- C12M21/02—Photobioreactors
-
- C—CHEMISTRY; METALLURGY
- C12—BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
- C12M—APPARATUS 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
- C12M23/00—Constructional details, e.g. recesses, hinges
- C12M23/02—Form or structure of the vessel
- C12M23/06—Tubular
-
- C—CHEMISTRY; METALLURGY
- C12—BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
- C12M—APPARATUS 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
- C12M23/00—Constructional details, e.g. recesses, hinges
- C12M23/44—Multiple separable units; Modules
-
- C—CHEMISTRY; METALLURGY
- C12—BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
- C12M—APPARATUS 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
- C12M29/00—Means for introduction, extraction or recirculation of materials, e.g. pumps
- C12M29/02—Percolation
Landscapes
- Health & Medical Sciences (AREA)
- Life Sciences & Earth Sciences (AREA)
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Wood Science & Technology (AREA)
- Organic Chemistry (AREA)
- Bioinformatics & Cheminformatics (AREA)
- Zoology (AREA)
- Genetics & Genomics (AREA)
- Biotechnology (AREA)
- Microbiology (AREA)
- Sustainable Development (AREA)
- Biomedical Technology (AREA)
- Biochemistry (AREA)
- General Engineering & Computer Science (AREA)
- General Health & Medical Sciences (AREA)
- Clinical Laboratory Science (AREA)
- Physics & Mathematics (AREA)
- Analytical Chemistry (AREA)
- Thermal Sciences (AREA)
- Molecular Biology (AREA)
- Apparatus Associated With Microorganisms And Enzymes (AREA)
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
The utility model relates to the device that little algae is cultivated production, particularly is applicable to the device of the cultivation production of spirulina photosynthetic response and algal biomass.
Blue-green algae spirulina (Blue-green Alga, Spirulina Spp.) is a kind of novel microprotein resource.This algae is recommended as " human optimal food " owing to contain the nutrient substance of multiple human body needs such as very high protein, amino acid, VITAMIN, unsaturated fatty acids, polysaccharide and mineral substance by Food and Argriculture OrganizationFAO (FAO), industrial development tissue (UNIDO) etc.1985,, take the lead in having set up first batch production Da Chi of China and cultivate production system with academy of agricultural sciences, the Jiangxi Province spirulina subject study group headed by the inventor.After this, similarly device is promoted in the whole nation.Da Chi cultivates and to have that floor space is big, cost of investment is high, energy consumption is big and the problem such as be subjected to that climate influences of production throughout the year.In recent years, CN1098246A releases a kind of spirulina production method and device, and it adopts irrigation canals and ditches to add stirring means; Other has a kind of CN2084288U spirulina enclosed streamline breeding device, and it adopts transparent plastic film tube, the method for blowing air in pipe.These methods are compared with conventional Da Chi production standard, and the former still exists floor space big, produce problems such as being subjected to the climate condition influence; The latter is still unresolved when SPIRULINA CULTIVATION, because the oxygen intoxication problem of accumulating that the photosynthetic product oxygen of frustule takes place, and the pipeline technical problems such as difficulty and Winter protection difficulty of when summer high temperature, dispelling the heat.Problems such as above standard also because pipeline is the plane laying, has only the upper strata single face can be subjected to light, therefore still exists light-receiving area little, and the efficiency of light energy utilization is not high.
The purpose of this utility model, be to overcome the problems referred to above that exist in the existing spirulina production technology standard, it is very little to design a kind of floor space, energy controlled temperature and illumination, but all-weather production, can carry out high-level efficiency photosynthesis, can in time supply with and make full use of carbonic acid gas, can in time discharge the photosynthetic reactor of the oxygen that produces in the photosynthetic response process.With this reactor multiple-unit combination, can carry out mcroorganism amount continuous production, be particularly useful for production higher-grade food, doctor
The industrialized unit of medicine level spirulina.
The purpose of this utility model adopts following design implementation:
Photosynthetic reactor of the present utility model is made of photosynthetic response tower and three-dimensional double flat spin formula pipeline.The body of the tower of this reactor and pipeline are made of the height light transmissive material.Be provided with venting hole at the body of the tower top in order to get rid of oxygen, reacting pipe is introduced by tower top in the drain pipe upper end, and the drain pipe lower end places the middle and lower part of tower, liquid-inlet pipe is introduced the tower from the top of tower, the bubbling plate is established at the tower middle part, establishes heat exchanger in the tower bottom, is provided with CO at tower bottom
2Air injection pipe, the design are taked three-dimensional double flat spin formula closed circulation pipeline, are furnished with suction pump, liquid-outlet valve and leakage fluid dram.
Effect of the present utility model is remarkable, and it has overcome, and conventional Da Chi production standard floor space is big, and energy consumption is big, and productive rate is low, and can not be golden the weather drawback of producing.It can provide the required luminous energy of photosynthetic response, fully satisfy frustule to CO by the comprehensive natural light that utilizes
2Needs, and can in time discharge dissolved oxygen in the deleterious nutrient solution, also owing to be provided with cold/heat exchanger controlled temperature, so the production efficiency height, this reactor can be stopped infecting of all the extraneous heteroplasia things and the various chemical pollution factors owing to be that totally enclosed circulation continuous production is cultivated.So sanitary condition is good, is specially adapted to production higher-grade food, pharmaceutical grade product.
The drawing explanation:
Fig. 1. the utility model photosynthetic reactor synoptic diagram.
Further specify the utility model below in conjunction with accompanying drawing and embodiment.
1, venting hole 2, drain pipe
3, liquid-inlet pipe 4, tower
5, bubbling plate 6, inlet mouth
7, cold/hot water outlet 8, heat exchanger
9, cold/hot water import 10, CO
2Air injection pipe
11, drawing liquid valve 12, suction pump
13, leakage fluid dram 14, liquid-outlet valve
15, flat spin formula pipeline
As seen from the figure, this reactor constitutes (omitting the partly middle of pipeline among the figure) by reaction tower and double flat spin formula reacting pipe.Reactor body of the tower and pipeline are made of the high transmission rate material.Top at tower 4 is provided with venting hole, in order to get rid of the oxygen that is produced in the photosynthetic response, reacting pipe is introduced in drain pipe 2 upper ends from tower top, the lower end places the tower middle and lower part, liquid-inlet pipe 3 is introduced in the tower on the top of tower 4, tower 4 pars intermedias are provided with bubbling plate 5, are provided with heat exchanger 8 in tower 4 bottoms, are provided with CO at tower bottom
2Air injection pipe 10, three-dimensional double flat spin formula closed conduct 15 upper and lower ends link to each other with reaction tower, are provided with leakage fluid dram 13, drawing liquid valve 11 and suction pump 12 on the bottommost pipeline of helical pipe 15.
The operational process of the utility model photosynthetic reactor is as follows: the cultivation algae and the algae liquid that actively carry out photosynthetic response in vertical double flat spin formula pipeline 15, drawing liquid valve 11 enters suction pump 12, by liquid-inlet pipe 3 bottom flowing through, be evacuated to the top of reaction tower 4, pouring is annotated and is descended.Spirulina algae liquid is at tower 4 middle parts, and the gas that is subjected to being entered by air inlet port 6 (by the bubbling plate 5 jet stirring that makes progress) is got rid of the oxygen in the nutrient solution rapidly.Reaction tower 4 also continues to provide the required luminous energy of algae growth and breeding to reach by CO simultaneously
2A large amount of CO that air injection pipe 10 enters
2Gas enlivens photosynthetic response and carries out.In summer, a large amount of heats of accumulating in photosynthetic reactor after the heat absorption (sending cold water to by bottom water inlet pipe 9) by heat exchanger 8, flow out from the top water outlet.Nutrient solution in the photosynthetic reactor is through drain pipe 2, and tapping valve 14 enters into flat spin formula pipeline 15.In pipeline 15, spirulina is active to carry out growth and breeding, and cell is bred in a large number and produced a large amount of oxygen, and nutrient solution flows into reaction tower through suction pump then once more from the bottom pipe that flows to suitable for reading of double flat spin formula pipeline 15, and circulation goes round and begins again.When the cultivation algae reaches certain optical density(OD), can discharge from bottom pipe leakage fluid dram 13 and gather.
Claims (3)
1, a kind of spirulina photosynthetic reactor, constitute by reaction tower (4) pipeline (15) and suction pump (12), it is characterized in that: the top at tower (4) is provided with venting hole, reacting pipe is introduced in drain pipe (2) upper end from tower top, the lower end places the tower middle and lower part, and liquid-inlet pipe (3) is introduced in the tower on the top of tower (4), and the pars intermedia of tower (4) is provided with bubbling plate (5), be provided with cold/heat exchanger (8) in tower (4) bottom, be provided with CO at tower bottom
2Air injection pipe (10), body of the tower links to each other with riser (15), and the bottommost pipeline of pipeline (15) is provided with leakage fluid dram (13), drawing liquid valve (11) and suction pump (12).
2, photosynthetic reactor according to claim 1 is characterized in that: pipeline (15) adopts three-dimensional double flat spin formula enclosed construction.
3, according to claim 1,2 described photosynthetic reactor, it is characterized in that: body of the tower (4) and double flat spin formula pipeline (15) are made of light transmissive material.
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 (1)
Publication Number | Publication Date |
---|---|
CN2234443Y true CN2234443Y (en) | 1996-09-04 |
Family
ID=33867694
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN95219504U Expired - Fee Related CN2234443Y (en) | 1995-07-31 | 1995-07-31 | Spirulina photosynthesis reactor |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN2234443Y (en) |
Cited By (15)
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 |
-
1995
- 1995-07-31 CN CN95219504U patent/CN2234443Y/en not_active Expired - Fee Related
Cited By (21)
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 |
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 |
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 |
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 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
CN2234443Y (en) | Spirulina photosynthesis reactor | |
CN101870953B (en) | Method for culturing microalgae | |
CN101597567B (en) | Photobioreactor | |
CN102206570B (en) | Apparatus and cultivating method for scaled cultivation of microalgae | |
CN102382755B (en) | Microalgae culturing device and microalgae culturing method | |
CN1213139C (en) | Photosynthesis bioreactor system for industrial production of micro algae | |
CN101748054B (en) | Photobioreactor for cultivating microalgae | |
EP2412794A1 (en) | Method for circulatory cultivating photosynthetic microalgae | |
CN107189930A (en) | Indoor microalgae culture system and its cultural method | |
CN101906380B (en) | Seal type pipeline culture device of bait microalgae and microalgae pipeline culture method | |
CN202246642U (en) | Coupling type photobiological reactor system | |
CN1966660A (en) | Device and method for large scale culturing Haemotococcum pluvies and converting astaxanthin | |
US20120021496A1 (en) | Method for circulatory cultivating photosynthetic microalgae | |
CN201729830U (en) | Sealed pipeline culturing device for bait microalgae | |
CN2688718Y (en) | Spiral pipe optical biological reactor | |
CN111676126B (en) | Airlift photobioreactor for microalgae culture | |
CN101353619B (en) | Algae microbe photosynthetic response system | |
CN106635768B (en) | Biological microalgae photosynthetic reactor and its application method | |
TW200932903A (en) | Process and system for photosynthesis of alga microorganisms | |
CN201864717U (en) | Three-phase reactor of photosynthetic heterotrophic algae | |
CN102168010A (en) | Photobioreactor for culturing microorganisms | |
CN102344889A (en) | Method for cyclic culture of photosynthetic microalgae | |
CN108285859B (en) | Novel pneumatic nostoc algae runway pond culture system | |
CN106244426A (en) | High density Large-scale microalgae culture apparatus | |
CN1208451C (en) | Closed pipeline type photosynthetic reactor |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
C14 | Grant of patent or utility model | ||
GR01 | Patent grant | ||
C19 | Lapse of patent right due to non-payment of the annual fee | ||
CF01 | Termination of patent right due to non-payment of annual fee |