KR101243110B1 - photobioreactor - Google Patents
photobioreactor Download PDFInfo
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- KR101243110B1 KR101243110B1 KR1020100098993A KR20100098993A KR101243110B1 KR 101243110 B1 KR101243110 B1 KR 101243110B1 KR 1020100098993 A KR1020100098993 A KR 1020100098993A KR 20100098993 A KR20100098993 A KR 20100098993A KR 101243110 B1 KR101243110 B1 KR 101243110B1
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- light
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- light guide
- reaction vessel
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- 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
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- 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
- C12M23/04—Flat or tray type, drawers
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- 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
- C12M31/00—Means for providing, directing, scattering or concentrating light
- C12M31/02—Means for providing, directing, scattering or concentrating light located outside the reactor
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- Wood Science & Technology (AREA)
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- Apparatus Associated With Microorganisms And Enzymes (AREA)
Abstract
The present invention provides a microalgae culture photobiological incubator and plate-shaped reaction vessels installed at predetermined intervals to allow microalgae to be cultured therein; It is provided on the reaction vessel is provided with a light concentrating unit for condensing sunlight and a light irradiation unit for irradiating the reaction vessel with light collected by the light condensing unit to irradiate light to the reaction vessel.
Description
The present invention relates to an optical bioreactor for mass cultivation of microalgae, and more particularly, to an optical bioreactor having improved light irradiation structure using sunlight in the photobioreactor.
Recently, as industrial emission CO is regarded as the main culprit of global warming, research is being actively conducted to utilize microalgae to fix CO₂.
Microalgae can play a role in the treatment of wastewater, immobilization of carbon dioxide, etc., due to their various capabilities, and have been used for the production of useful substances such as fuels, cosmetics, feed, food coloring and pharmaceutical raw materials. In the meantime, useful and high value added substances are constantly being discovered and expanding their applications.
There are many factors such as the composition of the medium, temperature, pH, light intensity, light quantity, etc., which affect the increase in the biomass and useful products of the microalgae, but among them, light occupies the largest share. In general, a device for culturing photosynthetic microalgae for the purpose of immobilizing carbon dioxide can be largely divided into a mass culture (open system) and a photobioreactor (closed system) outdoors. Outdoor mass cultivation apparatus including pond type has been mainly used in the form of reaction facilities such as lakes or large ponds and is commercially available in some countries.
However, this type of cultivation facility has the advantages of low initial investment and easy maintenance, but it is difficult to contaminate, isolate and purify, low cell concentration, high mass (especially nitrogen source), high water quality and quantity demand, and irregular climate. Due to problems such as conditions, expensive labor costs, the installation is extremely limited. In particular, the effective growth of light is not achieved inside the culture apparatus, the growth rate of the cells is low, the growth yield of the cells is low, and a large installation space is required to remove a large amount of carbon dioxide.
In order to solve the problems of such an outdoor mass culture apparatus, a high-concentration culture is carried out through a small-sized reactor to produce an amount equal to or greater than that of the outdoor mass culture apparatus, .
Currently developed forms include general stirred reactors, plate reactors, tubular reactors, column reactors, etc., and in all these types of reactors, efficient transmission of light is the most important point in reactor design. When the concentration of microalgae cells is low, medium and gas injection are the most important factors for cell proliferation, but when the high concentration is reached, the brightness is the most important factor. This is because the higher the concentration, the shorter the light transmission length.
That is, the light applied while the microalgae is incubated becomes more and more bulky as the microalgae grows, so that the microalgae on the surface of the reactor can continue to receive light, but the microalgae inside the reactor are microalgae on the surface. Because of the shadow effect will not be able to receive enough light to grow. However, most of the microalgae photobioreactors designed to date do not overcome this point, and thus the production efficiency thereof is lower than that of other microbial bioreactors. To overcome this and to transmit light efficiently. Recently, photobioreactors using internal light sources have been studied. Widely used photobioreactors include tubular photoreactors and panel photoreactors that use sunlight as an external light source. The reactor has a structure in which the narrow and long rectangular or cylindrical pipes are densely adhered to circulate the culture in order to maximize the irradiation area exposed to sunlight and to shorten the light transmission distance into the culture.
Such photobioreactors have advantages and disadvantages in their respective forms. In particular, the reactor using the fiber as the internal light source has a good light efficiency, but there is a problem that the cells adhere to the surface of the optical fiber. In addition, in the case of using a light source such as a fluorescent lamp as an internal light source, there is a problem in that the device must be operated continuously and accordingly excessive use of electricity (energy) is not efficient.
In order to solve this problem, Korean Patent No. 0933741 discloses a photobioreactor for culturing microalgae. The disclosed reactor uses an LED, a flexible LED, and has a structure in which the light source is directly in contact with the culture solution. In such a structure, micro algae are attached to the surface of the light source, thereby reducing light efficiency.
In addition, Korean Patent Publication No. 10-2009-0055170 discloses a semi-cylindrical photobiological reactor, and Korean Patent Registration No. 10-0897019 discloses an optical bioreactor for culturing microalgae with high efficiency. This reactor has a structure in which sunlight is irradiated to the photobioreactor using a reflective collector and an optical fiber. US Patent Application No. 2009/0211150 discloses a technical configuration for producing biomass and biodiesel by culturing microalgae Gloella in high concentration using a tubular photobioreactor, and US Patent Application No. 2005/0255584 In order to improve the light efficiency, a tubular photobioreactor having a surface area increased while using a partition of a transparent material is disclosed.
U.S. Patent No. 595876 discloses a tubular photobioreactor using a complex parabolic concentrator to improve the light collection efficiency of sunlight.
The present invention is to solve the above problems, to prevent the microalgae attached to the interior of the reaction vessel, and maximize the photovoltaic and LED light source irradiation efficiency of microalgae cultivation optical bioreactor that can increase the productivity of microalgae To provide.
The microalgae cultivation optical bioreactor of the present invention for achieving the above object is a plate-like reaction vessel that is installed at predetermined intervals so that the microalgae can be cultured therein; A light concentrating unit installed on the reaction vessel and condensing sunlight, and a light irradiation unit for irradiating the plate-shaped reaction vessel with light collected by the condensing unit to irradiate light to the reaction vessel. It is characterized by.
In the present invention, the light irradiation unit includes a plate-shaped light guide plate provided to correspond to the reaction vessel, and a reflection plate provided on the rear surface of the light guide plate. It is provided on the edge of the light guide plate and provided with a lamp module for irradiating light on the plate through the light guide plate.
The light irradiation unit includes a light guide plate having first and second light guide parts positioned between the reaction vessels, a reflection plate installed between the first and second light guide parts to reflect light to both sides of the first and second light guide parts, and It is provided on the side of the first and second light guide portion and provided with a lamp module for irradiating light to the plate-shaped reaction vessel through the first and second light guide portion.
The light collecting unit includes a Fresnel lens unit or a focusing lens unit installed on the light irradiation unit in the longitudinal direction of the plate-shaped photoreactor. The light collecting unit may be a light collecting lens unit installed on the light irradiation unit in the longitudinal direction of the plate-shaped photoreactor, and the light collecting lens unit may be a fresnel lens.
In the present invention, there is further provided a solar tracking unit for tracking the light collecting lens unit in the east-west direction and north-south direction along the sun.
The microbial photoreactor for culturing the microalgae according to the present invention maximizes the light source irradiation efficiency by using sunlight and a light emitting diode to increase the productivity of the microalgae, and the microalgae adhere to the surface of the light tank means that the light irradiation efficiency is lowered. It can be prevented fundamentally. The photobioreactor collects light while following the sun, and the collected light can be irradiated onto the plate-shaped reaction vessel through the light guide plate.
1 is a perspective view of a photobioreactor according to the present invention,
2 is a perspective view showing an extracting light collecting unit and light irradiation unit;
3 is a cross-sectional view showing a coupling relationship between a light guide plate and a lamp module;
4 is a perspective view showing another embodiment of a lamp module;
5 is a perspective view showing another embodiment of a light converging unit and a light irradiation unit;
6 and 7 are perspective views showing embodiments of the light collecting unit,
8 is a perspective view showing another embodiment of a light converging unit and a light irradiation unit;
9 is a perspective view illustrating a tracking unit for tracking a light collecting unit;
10 is a perspective view showing another embodiment of a tracking unit for tracking the light collecting unit.
1 to 4 show an optical bioreactor for culturing microorganisms in one embodiment of the present invention.
Referring to the drawings, the
The carbon
The plate-
And the
The
Referring to the drawings, the
In addition, the
Here, the
The lamp module for irradiating light to the
5 shows another embodiment of the light irradiation unit according to the present invention. The same components as in the above embodiment indicate the same reference numerals.
Referring to the drawings, the light irradiation unit is installed between the plate-shaped
A diffusion pattern may be formed on the opposing surfaces of the first and second light guides 56a and 56b as described above, and the first and second sides of the
On the other hand, the light guide plate may be made of a single double-sided light guide plate that can irradiate the light collected by the light collecting unit on both sides.
A
The
The
On the other hand, the
In the
In addition, since the weather is weak during the rainy or rainy season, the light emitting diode of the
On the other hand, the gas in the process of culturing the microalgae may use air, and when the supply of oxygen or carbon dioxide (CO2) can be supplied to these gases. Carbon dioxide can be supplied by mixing 5-20% with a separate gas (eg air).
In addition, the
As described above, the photobioreactor of the present invention is an optical bioreactor for mass production of microalgae using a plate-shaped light source that focuses sunlight and applies a light source capable of emitting strong light. It is possible to control the production of the production and to increase the spatial efficiency. In addition, when it is necessary to replace the light source during the cultivation to adjust the light intensity or maintenance of the light source, it is easy to replace it is advantageous to maintain a sterile state.
While the present invention has been particularly shown and described with reference to exemplary embodiments thereof, it is evident that many alternatives, modifications and variations will be apparent to those skilled in the art. Accordingly, the true scope of the present invention should be determined by the technical idea of the appended claims.
10; Photobioreactor
11; frame
30; condensing unit
40; tracking unit
50; light irradiation unit
Claims (8)
And a light irradiation unit for irradiating the plate-shaped reaction vessel with the light collected by the light collecting unit to irradiate light to the plate-shaped reaction vessel,
The light irradiation unit is provided to correspond to the reaction vessel of the plate and comprises a plate-shaped light guide plate in which the light collected by the light collecting unit is incident on the upper side side, and a reflecting plate is provided on the back surface of the light guide plate,
And a lamp module installed at an edge of the light guide plate to irradiate light to the plate-shaped reaction vessel through the light guide plate.
A condensing unit installed on the plate-shaped reaction vessel and condensing sunlight;
And a light irradiation unit for irradiating the plate-shaped reaction vessel with the light collected by the light collecting unit to irradiate the plate-shaped reaction vessel with light.
The light irradiation unit includes a light guide plate having first and second light guide portions positioned between the plate-shaped reaction vessels, and a reflection plate provided between the first and second light guide portions to reflect light to both sides of the first and second light guide portions. And a lamp module installed at a side of the first and second light guide parts to irradiate light to the plate-shaped reaction vessel through the first and second light guide parts.
The upper surface of the light guide plate is a microalgae culturing optical bioreactor, characterized in that the diffusion lens portion for diffusing the focused light into the light guide plate is formed.
Light reflecting grooves of a predetermined pattern is formed on the rear surface of the light guide plate.
The condensing unit is a microalgae culturing optical microbial culture, characterized in that provided with a Fresnel lens unit or a focusing lens unit installed on top of the light irradiation unit in the longitudinal direction of the plate-shaped photoreactor.
And a tracking unit for tracking the light collecting unit in the east-west direction and the north-south direction along the sun, or sliding the light-converging unit in a turbulent direction with the upper surface of the light guide plate.
Priority Applications (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
KR1020100098993A KR101243110B1 (en) | 2010-10-11 | 2010-10-11 | photobioreactor |
PCT/KR2011/007466 WO2012050325A2 (en) | 2010-10-11 | 2011-10-10 | Photobioreactor |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
KR1020100098993A KR101243110B1 (en) | 2010-10-11 | 2010-10-11 | photobioreactor |
Publications (2)
Publication Number | Publication Date |
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KR20120037313A KR20120037313A (en) | 2012-04-19 |
KR101243110B1 true KR101243110B1 (en) | 2013-03-12 |
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Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
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KR1020100098993A KR101243110B1 (en) | 2010-10-11 | 2010-10-11 | photobioreactor |
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KR (1) | KR101243110B1 (en) |
WO (1) | WO2012050325A2 (en) |
Families Citing this family (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
KR101290256B1 (en) * | 2012-07-11 | 2013-07-26 | 조선대학교산학협력단 | Aquarium with microalgea feeding device using the flat panel photobioreactor |
KR101319241B1 (en) * | 2012-12-10 | 2013-10-16 | 조선대학교산학협력단 | photobioreactor |
KR101452254B1 (en) * | 2013-02-04 | 2014-10-23 | 한국에너지기술연구원 | Floating-type Photobioreactor |
DK2923754T3 (en) * | 2014-03-26 | 2019-11-11 | Corning Inc | Modular photochemical flow reactor system |
WO2018223242A1 (en) * | 2017-06-09 | 2018-12-13 | Jianwei Chen | Production process for high purity algae |
CN111108185A (en) * | 2017-08-16 | 2020-05-05 | 日本曹达株式会社 | Microorganism culture system |
KR102700544B1 (en) * | 2023-04-24 | 2024-09-02 | 고성호 | LED(Light Emitting Diode) cell culture device |
Citations (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
KR100490641B1 (en) | 2003-12-16 | 2005-05-19 | 인하대학교 산학협력단 | Multiple layer photobioreactors and method for culturing photosynthetic microorganisms using them |
US20090047722A1 (en) * | 2005-12-09 | 2009-02-19 | Bionavitas, Inc. | Systems, devices, and methods for biomass production |
KR20090038313A (en) * | 2007-10-15 | 2009-04-20 | 주식회사 바이오트론 | High efficiency photo-bioreactor for culturing micro algae |
KR20090050940A (en) * | 2007-11-16 | 2009-05-20 | 히다치 가세고교 가부시끼가이샤 | Light guide plate and backlight unit |
Family Cites Families (5)
Publication number | Priority date | Publication date | Assignee | Title |
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US5023016A (en) * | 1987-03-16 | 1991-06-11 | King Industries, Inc. | Thermally stable sulfonate compositions |
US5877131A (en) * | 1997-08-25 | 1999-03-02 | Nch Corporation | Translucent lubricant |
US6919300B2 (en) * | 1999-07-15 | 2005-07-19 | Ashland Inc. | Penetrating lubricant composition |
US7745382B2 (en) * | 2005-01-18 | 2010-06-29 | Bestline International Research Inc. | Synthetic lubricant additive with micro lubrication technology to be used with a broad range of synthetic or miner host lubricants from automotive, trucking, marine, heavy industry to turbines including, gas, jet and steam |
US8022020B2 (en) * | 2005-01-18 | 2011-09-20 | Bestline International Research, Inc. | Universal synthetic penetrating lubricant, method and product-by-process |
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2010
- 2010-10-11 KR KR1020100098993A patent/KR101243110B1/en not_active IP Right Cessation
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2011
- 2011-10-10 WO PCT/KR2011/007466 patent/WO2012050325A2/en active Application Filing
Patent Citations (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
KR100490641B1 (en) | 2003-12-16 | 2005-05-19 | 인하대학교 산학협력단 | Multiple layer photobioreactors and method for culturing photosynthetic microorganisms using them |
US20090047722A1 (en) * | 2005-12-09 | 2009-02-19 | Bionavitas, Inc. | Systems, devices, and methods for biomass production |
KR20090038313A (en) * | 2007-10-15 | 2009-04-20 | 주식회사 바이오트론 | High efficiency photo-bioreactor for culturing micro algae |
KR20090050940A (en) * | 2007-11-16 | 2009-05-20 | 히다치 가세고교 가부시끼가이샤 | Light guide plate and backlight unit |
Also Published As
Publication number | Publication date |
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WO2012050325A3 (en) | 2012-06-07 |
KR20120037313A (en) | 2012-04-19 |
WO2012050325A2 (en) | 2012-04-19 |
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