WO2011102593A2

WO2011102593A2 - Photobioreactor for high-density microalgae culturing, and a microalgae culturing and harvesting method using the same

Info

Publication number: WO2011102593A2
Application number: PCT/KR2010/008036
Authority: WO
Inventors: 오희목; 유찬; 김희식; 안치용; 이재연
Original assignee: 한국생명공학연구원
Priority date: 2010-02-18
Filing date: 2010-11-15
Publication date: 2011-08-25
Also published as: KR20110094830A; WO2011102593A3

Abstract

The present invention relates to a photobioreactor for high-density microalgae culturing, and to a microalgae culturing and harvesting method using the same, and more specifically relates to a photobioreactor for high-density microalgae culturing which allows low-cost, high quality, volume production of microalgae such as Scenedesmus sp., Chlorella sp. and Spirulina sp. that are useful in processing carbon dioxide and also in the production of, by way of example, biodiesel, feed additives and health supplements, and relates to a microalgae culturing and harvesting method using the same. To this end, provided is a photobioreactor for high-density microalgae culturing comprising: a microalgae culturing reactor which is made with a closed structure, and is formed with a culture-liquid discharge port in a predetermined position at the bottom end; a reactor stopper which is joined in a detachable fashion to the upper end of the microalgae culturing reactor; a culture-liquid inflow tube and an air discharge tube which are inserted into the reactor stopper so as to connect through to the inside of the microalgae culturing reactor; and an air injection part which is joined in a detachable fashion to the lower end of the microalgae culturing reactor, and is for supplying air or a combustion gas into the microalgae culturing reactor, and also provided is a microalgae culturing and harvesting method using the same.

Description

Photobioreactor for high density microalgae culture, and microalgae culture and harvesting method using the same

The present invention relates to a microalgae high density photobioreactor and a microalgae culture and harvesting method using the same, more specifically, Scenedesmus sp., Chlorella sp., Spirulina sp. Microalgae high density cultivation photobioreactor for realizing low cost, high quality and mass production of microalgae useful for the production of biodiesel, feed additives, health supplements, etc. Cultivation and harvesting method.

At present, more than 40,000 species of microalgae are known, and they are known as biomass with various characteristics.

These microalgae use the photosynthetic action to fix carbon dioxide in the atmosphere or combustion flue gas and simultaneously produce oxygen, especially high in protein and lipids, and contain essential amino acids, DHA and EPA. And fodder [Oh, HM, et al ., 2003, High-value material from microalgae].

In addition, chlorella, which is used for livestock wastewater treatment technology in microalgae, is known to have an excellent effect on the removal of nutrients such as nitrogen and phosphorus, which are the cause of green algae in lakes and streams [Gonzlez, C., et al ., 2008, Microalgae-based processes for the biodegradation of pretreated piggery wastewaters].

According to a recent study, Senedesmus in microalgae has a high growth rate even at high concentrations of carbon dioxide and not only treats carbon dioxide emitted to the atmosphere, but also has high attention as a source of biodiesel due to its high lipid content. Morais, MG, et al ., 2007, Isolation and selection of microalgae from coal fired thermoelectric power plant form biofixation of carbon dioxide].

As such, in order to mass produce industrially useful microalgae at low cost, the open-air reactors have been mainly used. However, the open-air reactors are difficult to control the culture conditions such as temperature, pH, and the like. There was a disadvantage that the culture fluid and microalgae are easily contaminated.

In addition, the outdoor open reactor is required to install a separate stirring device such as aberration, etc., even if the stirring device is installed, uniform stirring and gas exchange is difficult, there is a disadvantage that a lot of energy is consumed.

Due to the above reasons, the conventional outdoor open reactor is difficult to grow a high density of microalgae, low productivity of the microalgae, there is a problem that the quality is reduced.

In addition, the cost of harvesting microalgae from the culture solution takes about one third of the total production cost, and it is difficult to use the effective harvesting method of precipitation and flotation, which makes it difficult to simplify the economic production and production process.

The present invention has been studied in order to solve the conventional problems as described above, by minimizing the external contact to the culture medium, it is possible to minimize the incorporation of harmful microorganisms from the outside, and useful such as Scenedesmus sp. The purpose of the present invention is to provide a microalgae high density photobioreactor having a closed cylindrical diaphragm structure capable of cultivating large quantities of microalgae at high density purely to improve productivity and product quality, and a method of culturing and harvesting microalgae using the same. have.

In addition, the present invention by using the exhaust gas containing the photosynthetic carbon source for agitation and harvesting, the entire process can be made in one reactor to simplify the production process, reduce the production cost, and maximize the efficiency of harvesting by precipitation The purpose of the present invention is to provide a microalgae high density photobioreactor capable of mass culturing microalgae and a microalgae culture and harvesting method using the same.

One embodiment of the present invention for achieving the above object is: a microalgae culture reactor is made of a closed structure, the culture liquid outlet is formed at a predetermined position at the bottom; A reactor plug detachably coupled to the top of the microalgal culture reactor; A culture solution inlet tube and an air discharge tube inserted into the reactor stopper so as to communicate with the inside of the microalgal culture reactor; An air injection unit detachably coupled to a lower end of the microalgal culture reactor and supplying air or exhaust gas into the microalgal culture reactor; It provides a microalgae high density culture photobiological reactor, characterized in that configured to include.

Another embodiment of the present invention for achieving the above object comprises the steps of: injecting the culture solution in the microalgal culture reactor; Supplying exhaust gas, which is a carbon source of photosynthesis, into the reactor through an air injection unit formed at the bottom of the microalgal culture reactor; Culturing the microalgal culture solution in a closed microalgal culture reactor under predetermined culture conditions; Microalgae harvesting step through flocculation reaction using combustion exhaust gas after microalgae culture; It provides a microalgae culture and harvesting method using a microalgae high-density culture photobioreactor comprising a.

Through the above problem solving means, the present invention provides the following effects.

According to the present invention, by supplying a gas source containing a photosynthetic carbon source upward from the bottom through an air inlet installed at the bottom of the reactor for purely high density bulk culture of microalgae, inducing uniform agitation of the culture medium to maximize light utilization In addition, the air sparger installed in the air injection unit (air sparger) to make the size of the bubble fine and effectively dissolve the carbon source contained in the gas source in the culture medium can easily realize high density culture of microalgae.

In particular, in order to minimize the contact of the culture medium with the outside through the reactor of the present invention manufactured in a closed type, by attaching a filter unit to the air inlet by blocking the influx of protozoa and fungus adversely affecting microalgal culture from the outside, Pure cultures can be made to improve the quality of cultured microalgae.

In addition, the present invention can easily induce rapid and low speed agitation necessary for the precipitation reaction by adjusting the flow rate of the gas source supplied to the culture of the microalgae, the efficiency of the precipitation reaction is increased, the air injection pipe made with gas injection By applying the upper surface of the inclined structure to the aggregated cells are concentrated in the outlet portion can be more effectively harvested cultured cells.

In addition, after harvesting through the coagulation reaction, there is no need for a separate additional device for the treatment of coagulation filtrate (supernatant), and the coagulation filtrate can be reused as a culture medium in the reactor, so that water, nutrients, etc. required for culture Minimize the use of

In addition, by increasing the residence time of the air and gas supplied by installing a plurality of triangle septum (septum) in the reactor of the present invention by increasing the dissolved carbon dioxide dissolved in the exhaust (combustion) gas and at the same time by inducing vortex of the culture solution Increasing the stirring efficiency of the culture solution, it is possible to more stably perform high density culture of microalgae.

1 is a microalgae high density optical bioreactor according to the present invention, a perspective view showing a closed cylindrical photoreactor for high density pure culture of microalgae,

2a and 2b is a plan view and a side view of the air inlet of the microalgae high density optical bioreactor according to the present invention,

3 is a photograph of the air injection unit actually produced using an acrylic material,

Figure 4 is a photograph showing the appearance of the actual reactor made of acrylic material,

Figure 5 is a photo of high density culture of Senedus mousse by supplying combustion exhaust gas to the closed cylindrical photobioreactor of the present invention,

Figure 6 A is a photograph of the culture medium of the sensedmus cultured in the closed cylindrical photobioreactor of the present invention at × 200 magnification of the optical microscope, Figure B is a census cultured in a conventional open channel photobioreactor Photograph of the Desmus culture medium at × 100 magnification of an optical microscope,

Figure 7 is a photo of the sensedmus culture medium (left) and the coagulant (CaCl ₂ and FeCl ₃ ) incubated in the closed cylindrical photobioreactor of the present invention was added with aggregating reaction after stirring with the combustion flue gas (left) Right side),

8 is a view showing an example in which an air dispersing septum is installed inside another embodiment of the microalgae high density culture photobioreactor according to the present invention.

Hereinafter, preferred embodiments of the present invention will be described in detail with reference to the accompanying drawings.

The present invention is to improve the quality of the microalgae produced by blocking the influx of protozoa and fungi harmful to the growth of microalgae, the production of microalgae, the gas source containing a carbon source of photosynthesis air inlet By supplying through the air spaser attached to the gas source, it is possible to make the bubble size of the gas source fine, improve the gas exchange rate, improve the gas source dissolution rate, and maintain a high concentration of the carbon source in the culture solution. The use of a gas source for agitation allows the microalgae in the culture to be uniformly dispersed, thereby increasing the utilization of the light source and the permeation distance into the incubator, thereby increasing the photosynthetic efficiency, thereby allowing high density mass culture. have.

To this end, the photobioreactor according to the present invention is a photo-reactor (A column-type septum photobioreactor) having a cylindrical diaphragm structure, is manufactured in a closed type to minimize the contact area with the outside, and excellent light transmittance and durability It is made of acrylic material which is advantageous for movement.

1 is a schematic diagram of a closed cylindrical photobioreactor for high density pure culture of microalgae used in the present invention, and FIGS. 2A and 2B are plan and side views respectively illustrating an air injection unit. 3 is an actual picture of the air injection unit manufactured using the acrylic material, and FIG. 4 is a picture of the actual reactor made of the acrylic material.

The closed cylindrical photobioreactor of the present invention is a microalgae culture reactor 10, a reactor stopper 20 is coupled to the top of the microalgae culture reactor 10 is made of a closed structure having a diaphragm structure therein, It consists of three parts, such as air injection unit 30 coupled to the bottom of the microalgae culture reactor 10, microalgae culture reactor to favor the cleaning and transport and storage of the cylindrical photoreactor of the present invention ( From the reactor 10, the reactor plug 20 and the air injection portion 30 is manufactured in a removable structure.

Preferably, the microalgae cultivation reactor 10 is 1.5 m in length, 0.2 m in internal diameter, 47 L maximum culture volume, 40 L and the appropriate culture volume is produced to the standard.

In addition, at a predetermined lower surface side surface of the microalgae culture reactor 10, a culture solution outlet 12 is formed at the bottom of the incubator in order to quickly and easily harvest the microalgae concentrated after the aggregation reaction.

The reactor stopper 20 is detachably mounted on the top of the microalgal culture reactor 10.

At this time, the culture medium inlet tube 22 is inserted into the reactor stopper 20 so as to communicate with the inside of the microalgae culture reactor 10, and the culture solution lost by harvesting and evaporating through the culture medium inlet tube 22. Will be supplemented.

In addition, the reactor stopper 20 is installed to be in communication with the interior of the microalgae culture reactor 10 in addition to the culture medium inlet tube 22, the air discharge tube 24, the microalgae culture through the air discharge tube (24) The gas source used for microalgae cultivation in the reactor 10 is discharged to the outside.

The air injection unit 30 supplies a gas source upwardly from the bottom of the microalgal culture reactor 10 to induce the dissolution of the carbon source contained in the gas source and the agitation of the culture solution, and in particular, the center of the air injection unit 30. An air sparger disposed in the gas source makes the bubble size of the gas source fine so that the carbon source in the gas source can be dissolved in the culture medium with high efficiency.

In more detail, the air injection portion 30 has a skeleton of an air injection pipe 32 having a cylindrical shape having an inclined top surface, and the bottom of the air injection pipe 32 has a sealing and supporting function. It is attached to the pedestal 31 of a larger diameter, and also the inclined upper portion of the air injection pipe 32 is made of a structure attached to the air sparger (33) made of rock.

At this time, the reason why the upper portion of the air injection pipe 32 of the air injection unit 30 is formed to be inclined is that the microalgae condensed after aggregation in the microalgal culture reactor 10 is at the bottom of the microalgal culture reactor 10. It can be quickly discharged toward the culture medium outlet (12) formed.

In addition, the air injection unit 30 includes an air injection tube 34 which is horizontally inserted through one side of the pedestal 31 and extends vertically toward the inside of the air injection tube 32, and the air injection tube 34 At a predetermined position of), an air filter 35 is installed to block the inflow of bacteria and fungi harmful to the growth of the microalgae, so that the pure culture of the microalgae is achieved.

That is, the horizontal groove is inserted into the pedestal 31 so that the air injection tube 34 is horizontally inserted into the pedestal 31 and vertically extended to the air injection pipe 32 thereon, and the air injection tube 34 ) 0.2 μm air filter 35 is installed to block the influx of bacteria and fungi harmful to microalgae culture from the outside.

In particular, after the chemical and biological flocculant is treated in the culture medium for rapid and effective harvesting, the gas source (exhaust gas) containing the carbon source is passed through the microalgae culture reactor through the air injection tube 34 having the air filter 35 ( 10) can be supplied to induce flocculation reaction.

On the other hand, the rubber packing 36 is inserted into the outer upper surface of the air injection pipe 32 of the upper surface of the pedestal 31 along its circumferential direction.

Therefore, the bottom surface of the microalgae culture reactor 10 is pressed while contacting the rubber packing 36 of the pedestal 31 while simultaneously injecting the air injection pipe 32 through the inside of the lower end of the microalgae culture reactor 10. In the end, the microalgal culture reactor 10 is closed.

As such, the inner diameter of the air injection pipe 32 of the air injection unit 30 is manufactured in the same 0.2 m as the microalgae culture reactor 10, and the upper slope of the air injection pipe 32 as a rock The manufactured air sparger 33 is installed, and a micrometer having a 0.3 m size pedestal 31 is attached to the bottom of the air injection pipe 32 to induce a safe installation of the entire photobioreactor. By allowing the rubber packing of the pedestal 31 to be coupled while the bottom of the microalgae culture reactor 10 is in contact with each other, it is possible to prevent the culture solution in the microalgae culture reactor 10 from leaking.

On the other hand, as shown in 8 attached to the microalgae culture reactor 10 according to the present invention, by further installing a septum for air dispersion (50 septum), to extend the residence time of the exhaust gas, the size of the bubble Not only can it be made fine, but also by forming a vortex in the culture medium to increase the dissolved rate of carbon dioxide in the exhaust gas and improve the stirring efficiency of the culture medium, it is possible to improve the reliability of the high-density culture of the microalgae.

Preferably, the air dispersion diaphragm 50 is manufactured in a triangular plate-like structure, and attaches a plurality of them at equal intervals along the longitudinal direction thereof in the microalgal culture reactor 10.

Therefore, when the exhaust gas is supplied into the microalgae culture reactor 10 through the air injection tube 34 having the air filter 35, the residence time is further increased while the exhaust gas reaches the air dispersion diaphragm 50. By forming a vortex in the culture medium while making the bubble size finer, it is possible to further increase the carbon dioxide dissolution rate in the exhaust gas and to increase the stirring efficiency of the culture medium, and consequently to facilitate high-density culture of the microalgae. Can be done.

Hereinafter, the microalgal culture and harvesting method of the present invention made through the microalgae high density photobioreactor for the above-described configuration will be described through the following examples.

실시예EXAMPLE

Using the photobioreactor of the present invention prepared in the above configuration was used to culture the senedusem useful for biodiesel production and wastewater treatment, the culture solution of senedusemus BG11 medium of the composition shown in Table 1 below was used. .

Table 1

That is, the culture solution of Sededmus is introduced through the culture medium inlet tube 22 of the reactor stopper 20 mounted on the top of the microalgal culture reactor 10, and the air injection formed at the lower end of the microalgal culture reactor 10 Air was supplied into the reactor 10 through the air injection tube 34 of the part 30.

At this time, the air supplied to the air injection tube 32 passes through the air filter 35 mounted on the air injection tube 34, the inflow of bacteria and mold harmful to the microalgal culture from the outside is blocked.

In addition, through the air injection tube 34, as the carbon source of photosynthesis was supplied with the actual combustion gas discharged by containing 5.5% of carbon dioxide from the LPG gas-based boiler, the air sparger (33) As a result, the bubble size of the gas source was made fine so that the carbon source in the gas source was dissolved in the culture medium with high efficiency.

As the culture conditions, the temperature was maintained at 25 ℃ using a fluorescent lamp as an artificial light source in a constant temperature and humidity room, the brightness was to be 120 μmol / ㎡ / s.

By doing so, as shown in the accompanying FIG. 5 after a certain time, it was possible to observe the high density culture of Senedmusmus in 30 L culture medium in the microalgae culture reactor 10 of the present invention.

비교예Comparative example

Using the conventional open channel reactor, seneduseus was incubated under the same culture conditions as in Example.

시험예1Test Example 1

In order to compare the productivity for the mass cultured microalgae according to the above-described example, that is, Senedmus mousse, the maximum dry weight was compared with those of the sensedmus cultured from the conventional open channel reactor as a comparative example.

As a result, the maximum dry weight of the microalgae produced according to the embodiment of the present invention was 2.98 g / L, the maximum dry weight of the microalgae was 0.34 g / L in the open channel reactor of the comparative example, which is the The maximum dry weight in the closed cylindrical photoreactor was about 8.7 times higher, and it was found that high density culture was possible in the closed cylindrical photoreactor of the present invention.

시험예 2Test Example 2

In order to confirm the inflow of harmful protozoa and fungi, algae of other species, etc. from the outside into the microalgae cultured according to the above-described examples and comparative examples, the culture solution was confirmed using an optical microscope. As shown in FIG.

As shown in Figure 6 (A), in the closed cylindrical photobioreactor of the present invention, no other fungi, primary animals, algae, and the like except for Senedmus, the culture solution while maintaining the prototype of the cells I was able to confirm the predominance within.

On the other hand, as shown in Figure 6 (B), in the conventional conventional open-water reactor as a comparative example, a number of microorganisms, protozoa, and other algae presumed to be a fungus of the actual entity was observed, the growth state of the Senedus mousse abnormally in the culture medium No predominance at.

Therefore, based on the closed cylindrical photoreactor according to the present invention and the culture method using the same, it can be seen that high-density pure culture is possible compared to the conventional reactor and method.

시험예3Test Example 3

According to the embodiment described above, after the incubation of the microalgae in the closed cylindrical photoreactor of the present invention, in order to easily and quickly harvest the cells, a flocculant is added to the culture solution, and the combustion gas used for the culture is supplied. The culture was stirred uniformly to induce aggregation reaction.

That is, the flocculant CaCl ₂ and FeCl ₃ are simultaneously added to 30 L of the Senedusmus culture cultured at 2.98 g / L in the microalgal culture reactor 10 of the closed cylindrical photoreactor according to the present invention, and the air filter 35 Through the air injection tube (34) having a combustion gas (the actual combustion gas discharged by containing 5.5% of carbon dioxide from the LPG gas boiler) for a predetermined time to induce rapid stirring, and then the combustion gas After the supply was cut off and allowed to stand for 5 minutes, the result is as shown in FIG.

The left reactor of FIG. 7 is a closed cylindrical photobioreactor that does not induce agglutination, and it can be seen that no separation of the crude and the culture medium occurs, whereas the right reactor of FIG. 7 is the coagulant CaCl ₂ and FeCl _3. As a closed cylindrical photobioreactor inducing agglutination reaction by adding, the coarse particles were completely separated from the culture by sedimentation.

After the cultivation of such microalgae, the conventional harvesting process is generally collected by centrifugation and spontaneous sedimentation, but these conventional methods require expensive machinery and a long time, the rapid harvest of microalgae is not achieved, In addition, the conventional method of harvesting the coarse powder using coagulation requires agitation and settling time of the coagulating agent and the coagulant, but the coagulation reaction according to the present invention reduces the harvesting cost by using only the coagulant. In addition, it can be seen that by treating two coagulants simultaneously to induce a rapid aggregation reaction, it is possible to shorten the reaction time to within 5 minutes to quickly separate the microalgae from a large amount of culture.

In addition, in order to measure the efficiency of the aggregation reaction, the optical density (OD, optical density) of the upper culture layer before and after the aggregation reaction was measured at a wavelength of 680 nm, the aggregation efficiency was calculated using the following equation (1).

As a result of the calculation, the flocculation efficiency using the combustion gas in the photobioreactor of the present invention was very high, more than 99%, from which the coagulation harvesting method of the present invention can quickly and easily harvest the cultured microalgae, It can be simplified, and furthermore, no additional device is required for the treatment of the coagulation filtrate after the coagulation reaction, and the coagulation filtrate (supernatant) can be reused as a culture medium in the incubator to minimize the supply of water and nutrients necessary for the culture. Could.

(Explanation of the sign)

10 microalgae culture reactor 12 culture medium outlet

20: reactor stopper 22: culture fluid inlet tube

24: air discharge pipe 30: air injection unit

31: pedestal 32: air injection pipe

33: air sparger 34: air injection tube

35: air filter 36: rubber packing

50: diaphragm for air dispersion

Claims

The microalgae culture reactor 10 is made of a closed structure, the culture medium outlet 12 is formed at a predetermined position at the bottom;
A reactor stopper 20 detachably coupled to the top of the microalgal culture reactor 10;
A culture solution inlet tube 22 and an air discharge tube 24 inserted into the reactor stopper 20 so as to communicate with the inside of the microalgal culture reactor 10;
An air injection unit 30 detachably coupled to the lower end of the microalgal culture reactor 10 to supply air or exhaust gas into the microalgal culture reactor 10;
Microalgae high density culture photobiological reactor, characterized in that comprising a.
The method according to claim 1,
The microalgae high density culture photobiological reactor, characterized in that a plurality of air dispersion diaphragm 50 is installed at regular intervals along the vertical direction of the microalgae culture reactor (10).
The method according to claim 2,
The air dispersion diaphragm 50 is a microalgae high density culture bioreactor, characterized in that it is made of a triangular plate structure.
The method according to claim 1,
The microalgae culture reactor 10 has a length of 1.5 m, the inner diameter is 0.2 m, the maximum culture volume of 47 L, the appropriate culture volume 40 L, etc. Photobioreactor for.
The method according to claim 1,
The air injection unit 30 is:
An air injection pipe 32 press-fitted through the lower end of the microalgae culture reactor 10 having an inclined angle at an upper surface thereof;
An air sparger 33 attached to the inclined upper portion of the air injection pipe 32;
A larger diameter pedestal 31 which is integrally attached to the bottom of the air injection pipe 32;
An air injection tube 34 inserted horizontally through one side of the pedestal 31 and vertically extending toward the inside of the air injection pipe 32 to become a supply path of air or exhaust gas;
An air filter 35 mounted at a predetermined position of the air injection tube 34;
Microalgae high density culture photobiological reactor, characterized in that consisting of.
According to claim 5, Out of the upper surface of the pedestal 31, the outer surface of the air injection pipe 32 is inserted into the rubber packing 36 which the bottom surface of the microalgae culture reactor 10 in contact with the circumferential direction is inserted Photomicroorganism reactor for microalgae high density culture, characterized in that.
Injecting the culture solution into the microalgal culture reactor (10);
Supplying air upwardly into the reactor 10 through the air injection pipe 32 of the air injection unit 30 formed at the bottom of the microalgal culture reactor 10;
Supplying exhaust gas, which is a carbon source of photosynthesis, upward through the air injection pipe 32 of the air injection unit 30 formed at the bottom of the microalgal culture reactor 10;
Culturing the microalgal culture in the closed microalgal culture reactor 10 under predetermined culture conditions;
Microalgae harvesting step through flocculation reaction using combustion exhaust gas after microalgae culture;
Microalgae culture and harvesting method using a microalgae high density optical bioreactor for culturing.
The method according to claim 7,
When the air or the exhaust gas is supplied to the reactor 10, the micro-algae high density culture, characterized in that the bubble size of the air and gas source is made fine through the air sparger 33 is supplied into the reactor 10 Microalgae cultivation and harvesting method using photobioreactor.
The method according to claim 7,
When the air or the exhaust gas is supplied to the reactor 10, the microalgae high density culture microorganisms, characterized in that through the air filter 35 to block the inflow of bacteria and fungi harmful to the microalgal culture from the outside Microalgae culture and harvesting method using a reactor.
The method according to claim 7,
When the air or the exhaust gas is supplied to the reactor 10, the vortex is formed in the culture medium by the air dispersion diaphragm 50 in the microalgae culture reactor 10, characterized in that the microalgae high density culture bioreactor Microalgae culture and harvesting method using.
The method according to claim 7,
The culture conditions are microalgae cultivation and harvesting using a microalgae high density culture photobioreactor, characterized in that the luminous intensity of 120 μmol / ㎡ / s is irradiated from a fluorescent light as an artificial light source in a constant temperature and humidity room maintained at 25 ℃ Way.
The method according to claim 7,
The microalgal culture is a microalgae culture and harvesting method using a microalgae high density optical bioreactor, characterized in that the Senedusmus culture medium.
The method according to claim 7,
After the incubation of the microalgae, the flocculant is added to the culture medium, and further supplying the combustion gas used for the culture to induce flocculation reaction of the culture medium using the microalgae high density culture photobioreactor further comprising Microalgae Cultivation and Harvesting Methods.
The method according to claim 13,
Microalgae cultivation and harvesting method using a microalgae high density photobioreactor for the simultaneous addition of CaCl 2 and FeCl 3 as the flocculant.