CN100404661C - Vegetal alga, and system and method of microbe potosynthesis reaction - Google Patents
Vegetal alga, and system and method of microbe potosynthesis reaction Download PDFInfo
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- CN100404661C CN100404661C CNB2004100857425A CN200410085742A CN100404661C CN 100404661 C CN100404661 C CN 100404661C CN B2004100857425 A CNB2004100857425 A CN B2004100857425A CN 200410085742 A CN200410085742 A CN 200410085742A CN 100404661 C CN100404661 C CN 100404661C
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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
- C12M23/06—Tubular
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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
- C12M29/00—Means for introduction, extraction or recirculation of materials, e.g. pumps
- C12M29/14—Pressurized fluid
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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
- C12M31/08—Means for providing, directing, scattering or concentrating light by conducting or reflecting elements located inside the reactor or in its structure
Abstract
The present invention relates to a photosynthetic reaction system for vegetal alga and microbes and a method thereof, which causes the culture liquid of vegetal algae and microbes, which is injected into the system, to circularly carry out photosynthesis and deoxygenation. The photosynthetic reaction system for vegetal algae and microbes comprises a photosynthetic reaction unit, a pressurizing liquid delivering unit and a deoxygenation and regulation unit, wherein the photosynthetic reaction unit is a light transmission pipe passage, and the deoxygenation and regulation unit is composed of a deoxygenation cylinder, a liquid collecting cylinder, a regulating cylinder, etc. so as to be convenient for manufacture and assembly and form the effect of multiple deoxygenation, so that oxygen generated in the culture liquid is easily and rapidly discharged.
Description
Technical field
A kind of photosynthetic reaction system and method refer to a kind of vegetal alga and microbe photosynthetic response system and method especially.
Background technology
(spirulina contains the nutritive ingredient of multiple beneficial human bodies such as rich in protein, mineral substance and ferment in Spirulina) to blue-green algae, is widely recommended edible in recent years.The nutrient solution of blue-green algae is made competent photosynthesis satisfying the required nutrient of its frustule through a photosynthetic reaction system, and discharges the oxygen that is created in the nutrient solution, makes blue-green algae growth and breeding in large quantities.
Known blue-green algae photosynthetic reaction system is the big cultivation pool of an out of door.The nutrient solution of blue-green algae is contained in the big cultivation pool of this out of door, to carry out photosynthesis.The floor space of right this big cultivation pool is big, energy consumption is many, use is limited by the influence of weather, vulnerable to pollution and influence the quality of this blue-green algae especially, causes the many puzzlements of production dealer.
Known another kind of blue-green algae photosynthetic reaction system is addressed a kind of spirulina photosynthetic reactor as China Patent No. CN95219504.6, and it is made of a reaction tower and a vertical double flat spin formula pipeline.This reaction tower and this pipeline are that light-transmitting materials is made, so that the nutrient solution that flows in it carries out photosynthesis.In this reaction tower and be provided with devices such as a bubbling plate and a cool-heat-exchanger, be created on the oxygen in this nutrient solution and the temperature of this nutrient solution of control with discharge.This spirulina photosynthetic reactor mainly is to provide an enclosed recycle system, to overcome the variety of problems of known big cultivation pool.Right this spirulina photosynthetic reactor still have make complicated, cost is high, easy breakage, oxygen are difficult to be discharged from, the difficult control of temperature of nutrient solution is difficult in the clean and maintenance of demanding criteria and reaction tower so that reduce photosynthetic effect and influence problems such as the quality existence of blue-green algae, and discomfort is made industrial mass production.
As from the foregoing, above-mentioned known blue-green algae photosynthetic reaction system on actual manufacturing and using, is obviously had any problem and the defective existence, and is remained to be improved.
Summary of the invention
Main purpose of the present invention, be to provide a kind of vegetal alga and microbe photosynthetic response system and method, make that its required floor space reduces, the energy use reduce, running is not subjected to the influence of weather, especially can avoids contaminated to safeguard the fine quality of algae.
A time purpose of the present invention is to provide a kind of vegetal alga and microbe photosynthetic response system and method, makes the oxygen that is created in the nutrient solution be easy to promptly be discharged, and enhancing productivity, and is beneficial to industrial mass production.
Another object of the present invention is to provide a kind of vegetal alga and microbe photosynthetic response system and method, it is made and assembling cracky simply and not, to reduce required cost.
Another purpose of the present invention is to provide a kind of vegetal alga and microbe photosynthetic response system and method, makes it be easy to clean and maintenance, to guarantee the quality of photosynthetic effect and algae.
A further object of the present invention is to provide a kind of vegetal alga and microbe photosynthetic response system and method, makes it can control the temperature of nutrient solution effectively.
In order to reach above-mentioned purpose, the present invention is mainly providing a kind of vegetal alga and microbe photosynthetic response system, comprises a photosynthetic response unit, a pressure transfusion unit and a deoxygenation and regulon; This photosynthetic response unit is a printing opacity pipeline; The unitary inlet end of this pressure transfusion is communicated in the exit end of this printing opacity pipeline; This deoxygenation and regulon comprise the injection oxygen exhauster of a hollow and the liquid level regulation apparatus of a hollow, this injection oxygen exhauster comprises an oxygen discharging canister and a liquid cylinder that is connected with group, this oxygen discharging canister is provided with a fluid inlet, a venting port and a hollow tube wall on one, this fluid inlet is communicated in the unitary exit end of this pressure transfusion, should go up the top that venting port is positioned at this oxygen discharging canister, this hollow tube wall is from going up the inboard that venting port extends and be located opposite from this fluid inlet downwards, this liquid level regulation apparatus comprises that one regulates tube, this adjusting tube is communicated in this liquid cylinder, and the inlet end of this printing opacity pipeline is communicated in this adjusting tube; This injection oxygen exhauster comprises a vapor pipe, this exhaust stack is connected in this oxygen discharging canister, the stage casing of this oxygen discharging canister is provided with a necking part and a side venting port, this side venting port is positioned at the below of this necking part, the upper end of this vapor pipe is arranged in this hollow tube wall, and the lower end of this vapor pipe forms an enlarged portion and is located opposite from the inboard of this side venting port.By this, can make the oxygen that is created in the nutrient solution be easy to promptly be discharged.
By connecting to form of this photosynthetic response unit, this pressure transfusion unit and this deoxygenation and regulon, make the nutrient solution and the algae kind that flow into its interior vegetal alga and microorganism can be the sealing carrying out circularly of vertical three-dimensional multi coil road photosynthesis and deoxygenation, therefore, required floor space reduces, the energy uses minimizing, running is not subjected to the influence of weather and it is contaminated to safeguard the quality of the algae that produced to avoid; By this fluid inlet, the configuration of venting port and this hollow tube wall on this, make the oxygen that is created in the nutrient solution be easy to promptly be discharged, to enhance productivity; Become this injection oxygen exhauster by this oxygen discharging canister with this liquid cylinder winding, it is made and assembling cracky simply and not, to reduce required cost.By the winding of this oxygen discharging canister and this liquid cylinder, and the design of this printing opacity pipeline, make it be easy to clean and maintenance, to guarantee the quality of photosynthetic effect and algae.
In addition, vegetal alga of the present invention and microbe photosynthetic response system further comprise a heating unit, and this heating unit is connected between the exit end and the unitary inlet end of this pressure transfusion of this printing opacity pipeline.
In addition, vegetal alga of the present invention and microbe photosynthetic response system further comprise a watering unit, and this watering unit is positioned at the unitary top of this photosynthetic response.
By this heating unit and this unitary configuration of sprinkling water, make it can control the temperature of nutrient solution effectively.
In addition, the present invention is mainly providing a kind of vegetal alga and microbe photosynthetic response method, and its step comprises:
(1) provides a printing opacity pipeline, a pressure transfusion unit and a deoxygenation and regulon;
(2) inject a nutrient solution and algae kind in this printing opacity pipeline, it is interior to carry out photosynthesis and generation oxygen that this nutrient solution flows in this printing opacity pipeline, and this nutrient solution also flows to this pressure transfusion unit;
(3) open this pressure transfusion unit and flow to this deoxygenation and regulon, this nutrient solution is impacted in this deoxygenation and regulon splash shape to discharge oxygen to form a rotation spray diffusion to force this nutrient solution; And
(4) collect this nutrient solution in this deoxygenation and regulon, and aspirate this nutrient solution and flow in this printing opacity pipeline to carry out photosynthesis once more.
Reach technique means and the effect that predetermined purpose is taked for further setting forth the present invention, see also following about detailed description of the present invention and accompanying drawing, yet shown in accompanying drawing only provide with reference to and usefulness is described, be not to be used for the present invention is limited.
Description of drawings
The partial cutaway schematic of Fig. 1 vegetal alga of the present invention and microbe photosynthetic response system.
The schematic perspective view of the injection oxygen exhauster of Fig. 2 vegetal alga of the present invention and microbe photosynthetic response system.
The schema of Fig. 3 vegetal alga of the present invention and microbe photosynthetic response method.
Nomenclature among the figure:
1 photosynthetic response unit
10 straight tubes, 11 bend pipes
12 assist openings
2 pressure transfusion unit
20 transfer limes
3 deoxygenations and regulon
4 spray oxygen exhauster
40 oxygen discharging canisters, 401 fluid inlets
Venting port 403 hollow tube walls on 402
404 necking parts, 405 side venting ports
41 liquid cylinders, 42 vapor pipes
421 enlarged portion
5 liquid level regulation apparatus
50 exntension tubs, 501 pressure regulation openings
Cut following section of 503 exntension tubs on 502 exntension tubs
51 regulate tube
6 communication apparatus
60 cleaning valve assemblies
7 valve modules of gathering
8 heating units
80 heating tubes, 81 inlet switching parts
82 outlet switching parts
9 watering unit
Embodiment
See also illustrated in figures 1 and 2, a kind of vegetal alga of the present invention and microbe photosynthetic response system, with so that flow into vegetal alga in it and nutrient solution and the algae kind of microorganism, nutrient solution as blue-green algae, carry out photosynthesis and deoxygenation circularly, make blue-green algae growth and breeding in large quantities, to produce its contained various nutritive ingredients.This vegetal alga and microbe photosynthetic response system comprise a photosynthetic response unit 1, a pressure transfusion unit 2 and a deoxygenation and regulon 3, wherein:
Deoxygenation and regulon 3, it comprises the injection oxygen exhauster 4 of a hollow, the liquid level regulation apparatus 5 and a communication apparatus 6 of a hollow.
As shown in Figure 1 and Figure 2, this injection oxygen exhauster 4 comprises an oxygen discharging canister 40 and a liquid cylinder 41 that is connected with group, and it is made that this oxygen discharging canister 40 can be stainless steel, and it is made that this liquid cylinder 41 can be light-transmitting materials such as glass or acryl, so that make and assembling, so not as limit.The epimere of this oxygen discharging canister 40 is provided with a venting port 402 and a hollow tube wall 403 on the fluid inlet 401,, this fluid inlet 401 is communicated in the exit end of this pressure transfusion unit 2 with a transfer lime 20, should go up the top that venting port 402 is positioned at this oxygen discharging canister 40, this hollow tube wall 403 is from going up the inboard that venting port 402 extends and be located opposite from this fluid inlet 401 downwards.The stage casing of this oxygen discharging canister 40 is provided with a necking part 404 and a side venting port 405, and this side venting port 405 is positioned at the below of this necking part 404.This injection oxygen exhauster 4 comprises a vapor pipe 42 in addition, this vapor pipe 42 is connected in this oxygen discharging canister 40, the upper end of this vapor pipe 42 is arranged in this hollow tube wall 403, and the lower end of this vapor pipe 42 forms an enlarged portion 421 and is located opposite from the inboard of this side venting port 405.
This liquid level regulation apparatus 5 comprises exntension tubs 50 and an adjusting tube 51 that is connected with group, it is made that these exntension tubs 50 can be stainless steel, and can be divided into and cut following section 503 two combinations of 502 and one exntension tubs on the exntension tubs, conveniently to take the inwall that cleans these exntension tubs 50 and this adjusting tube 51 apart, it is made that this adjusting tube 51 can be light-transmitting materials such as glass or acryl, so that make and assembling, so not as limit.The top of these exntension tubs 50 is provided with a pressure regulation opening 501.
This communication apparatus 6 is connected in the bottom of this liquid cylinder 41 and the bottom of this adjusting tube 51, makes this adjusting tube 51 be communicated in this liquid cylinder 41.This communication apparatus 6 also has a cleaning valve assembly 60.The bending downwards of the inlet end of this printing opacity pipeline is communicated in this adjusting tube 51.
Vegetal alga of the present invention and microbe photosynthetic response system also comprise the valve module 7 of gathering.This valve module 7 of gathering is connected between the inlet end of the exit end of this printing opacity pipeline and this pressure transfusion unit 2, in order to draw the nutrient solution that flows in this printing opacity pipeline.
When using the implementation process of vegetal alga of the present invention and microbe photosynthetic response system, can inject the nutrient solution of a blue-green algae in this printing opacity pipeline by the assist openings 12 of this printing opacity pipeline, it is interior to carry out photosynthesis and generation oxygen that this nutrient solution flows in this printing opacity pipeline, and this nutrient solution also flows to this pressure transfusion unit 2.This nutrient solution also can inject this by the pressure regulation opening 501 of these exntension tubs 50 to be regulated in the tube 51.Open this pressure transfusion unit 2 and flow to this deoxygenation and regulon 3 from this printing opacity pipeline to force this nutrient solution.When this nutrient solution sprayed in this oxygen discharging canister 40 via this fluid inlet 401, this nutrient solution at first impacted in the oxygen discharging canister 40 of this deoxygenation and regulon 3 and is beneficial to oxygen from going up venting port 402 discharges to form a rotation spray shape; Then, this nutrient solution falls and is collected into this necking part 404 backs and impacts the enlarged portion 421 of these vapor pipes 42 and form the diffusion shape that splashes and be beneficial to oxygen and discharge from this side venting port 405; At last, this nutrient solution falls and is collected in this liquid cylinder 41, and oxygen is discharged from the upper end of this vapor pipe 42.So, can discharge most oxygen to promote the photosynthetic ability of this nutrient solution.Because this nutrient solution has generated saturated oxygenous liquid when passing through this oxygen discharging canister 40, be difficult for carrying out photosynthesis again, so this oxygen discharging canister 40 to can be light tight material such as stainless steel made; Discharged most oxygen when this nutrient solution is collected in this liquid cylinder 41 again, can proceed photosynthesis, thus this liquid cylinder 41 to can be light-transmitting materials such as glass made.So, make more simply and not cracky of the manufacturing of this oxygen discharging canister 40 and this liquid cylinder 41 and assembling.This nutrient solution is flowed through this communication apparatus 6 to this adjusting tube 51 o'clock, can temporarily open this cleaning valve assembly 60, to remove heavier settling, and this nutrient solution of test of also can sampling.But these pressure regulation opening 501 exhausts are to keep the pressure in this liquid level regulation apparatus 5; In addition, can aspirate the too much foam that is created in this liquid level regulation apparatus 5 by this pressure regulation opening 501; Again, can wear a supply pipe, to add the nutrient that carbonic acid gas etc. helps this nutrient solution growth and breeding from this pressure regulation opening 501.The pressure of this pressure transfusion unit 2 causes the negative pressure in this printing opacity pipeline, this nutrient solution is sucked up in this printing opacity pipeline, to carry out photosynthesis once more from this adjusting tube 51.When these liquid level regulation apparatus 5 interior nutrient solution water levels being risen, can adjust the output pressure of this pressure transfusion unit 2, to reduce this nutrient solution water level if the pressure in this printing opacity pipeline increases.So, can make this nutrient solution be the sealing of vertical three-dimensional multi coil road and carry out photosynthesis and deoxygenation circularly, to increase increasing of its nutritive ingredient.This nutrient solution also can be by this valve module 7 sampling test of gathering, and when this nutrient solution reaches the nutrient density of demand, can be discharged by this gather valve module 7 or this cleaning valve assembly 60 and be gathered.
Vegetal alga of the present invention and microbe photosynthetic response system further comprise a heating unit 8.This heating unit 8 is provided with several heating tubes 80, an inlet switching part 81 and an outlet switching part 82, and these heating tubes 80 are connected between the inlet end of the exit end of this printing opacity pipeline and this pressure transfusion unit 2 via this inlet switching part 81 and this outlet switching part 82.This heating unit 8 can manual or automatic induced mode heat the water that is placed in this heating unit 8, and the thermal energy transfer that makes water is to these heating tubes 80, to control the temperature of this nutrient solution.It is made that these heating tubes 80 can be stainless steel, to promote the effect and the wearing quality of heating.
Vegetal alga of the present invention and microbe photosynthetic response system further comprise a watering unit 9.This watering unit 9 is positioned at the top of this photosynthetic response unit 1, and can carry out the regularly watering of constant temperature in manual or automatic induced mode according to the demand of Working environment, to reduce the temperature of the nutrient solution in this printing opacity pipeline.
Therefore, see also Fig. 1 and shown in Figure 3, be a kind of vegetal alga of the present invention and microbe photosynthetic response method, its step comprises:
(1) provide a printing opacity pipeline, a pressure transfusion unit 2 and a deoxygenation and regulon 3: this printing opacity pipeline, this pressure transfusion unit 2 and this deoxygenation and regulon 3 are connected to form above-mentioned vegetal alga and microbe photosynthetic response system.
(2) inject a nutrient solution and algae kind in this printing opacity pipeline, this nutrient solution flows in this printing opacity pipeline to carry out photosynthesis and to generate oxygen, this nutrient solution also flows to this pressure transfusion unit 2: this printing opacity pipeline is a three-dimensional spiral fashion so printing opacity pipeline, therefore, this nutrient solution from top to bottom flows in this printing opacity pipeline in the mode of circulation in proper order, make this nutrient solution can absorb light fully to carry out photosynthesis, breeding rapidly.
(3) open this pressure transfusion unit 2 and flow to this deoxygenation and regulon 3, this nutrient solution is impacted in this deoxygenation and regulon 3 splash shape to discharge oxygen to form a rotation spray diffusion to force this nutrient solution:
(4) collect this nutrient solution in this deoxygenation and regulon 3, and aspirate this nutrient solution and flow in this printing opacity pipeline to carry out photosynthesis once more:
In addition, this step (two) further provides a heating unit 8, and this nutrient solution is flowed through behind this heating unit 8, flows to this pressure transfusion unit 2 again, to control the temperature of this nutrient solution.
In addition, this step (two) further provides a watering unit 9, and can sprinkle water according to the demand of Working environment on this printing opacity pipeline in this watering unit 9, to reduce the temperature of the nutrient solution in this printing opacity pipeline.
In addition, this step (four) provides the valve module 7 of gathering, and this nutrient solution is flowed through behind this printing opacity pipeline, draws this nutrient solution by this valve module 7 of gathering.
By above-mentioned vegetal alga and microbe photosynthetic response system and method, the present invention has following characteristics:
1, this photosynthetic response unit, this pressure transfusion unit and this deoxygenation and regulon connects to form, make the nutrient solution and the algae kind that flow into its interior vegetal alga and microorganism can be the sealing carrying out circularly of vertical three-dimensional multi coil road photosynthesis and deoxygenation, therefore, required floor space reduces, the energy uses minimizing, running is not subjected to the influence of weather and it is contaminated to safeguard the quality of the algae that produced to avoid.
2, this fluid inlet, the configuration of venting port and this hollow tube wall on this, and the configuration of this vapor pipe, this necking part and this side venting port, form repeatedly the effect of deoxygenation, make the oxygen that is created in the nutrient solution be easy to promptly be discharged, therefore, enhance productivity, and be beneficial to industrial mass production.
3, this oxygen discharging canister becomes this injection oxygen exhauster with this liquid cylinder winding, and this adjusting tube becomes this liquid level regulation apparatus with this exntension tubs winding, makes it make and assemble simply and cracky not, to reduce required cost.
4, the winding of this oxygen discharging canister and this liquid cylinder, and the design of this printing opacity pipeline make it be easy to clean and maintenance, to guarantee the quality of photosynthetic effect and algae.
5, this heating unit and the unitary configuration of should sprinkling water can be made suitable temperature regulation according to the difference of region, season, weather or according to the demand of nutrient solution, make it can control the temperature of nutrient solution effectively.
In sum, the present invention meets the important document of application for a patent for invention fully, so file an application according to patent law.The above, only be the detailed description and the accompanying drawing of specific embodiments of the invention, be not in order to restriction the present invention and feature of the present invention, such as have in the affiliated technical field and know the knowledgeable usually, modify or variation along the equivalence of doing according to spirit of the present invention, all should be contained in the claim of the present invention.
Claims (14)
1. vegetal alga and microbe photosynthetic response system comprise:
One photosynthetic response unit, it is a printing opacity pipeline;
One pressure transfusion unit, its inlet end is communicated in the exit end of this printing opacity pipeline; And
One deoxygenation and regulon, it comprises the injection oxygen exhauster of a hollow and the liquid level regulation apparatus of a hollow, this injection oxygen exhauster comprises an oxygen discharging canister and a liquid cylinder that is connected with group, this oxygen discharging canister is provided with a fluid inlet, a venting port and a hollow tube wall on one, this fluid inlet is communicated in the unitary exit end of this pressure transfusion, should go up the top that venting port is positioned at this oxygen discharging canister, this hollow tube wall is from going up the inboard that venting port extends and be located opposite from this fluid inlet downwards, this liquid level regulation apparatus comprises that one regulates tube, this adjusting tube is communicated in this liquid cylinder, the inlet end of this printing opacity pipeline is communicated in this adjusting tube, it is characterized in that:
This injection oxygen exhauster comprises a vapor pipe, this exhaust stack is connected in this oxygen discharging canister, the stage casing of this oxygen discharging canister is provided with a necking part and a side venting port, this side venting port is positioned at the below of this necking part, the upper end of this vapor pipe is arranged in this hollow tube wall, and the lower end of this vapor pipe forms an enlarged portion and is located opposite from the inboard of this side venting port.
2. vegetal alga as claimed in claim 1 and microbe photosynthetic response system, it is characterized in that, this photosynthetic response unit comprises a plurality of straight tubes and a plurality of bend pipe, and these straight tubes and these bend pipes are connected in series the three-dimensional spiral fashion so printing opacity pipeline that forms a double inclination at interval.
3. vegetal alga as claimed in claim 1 and microbe photosynthetic response system is characterized in that, this printing opacity pipeline is provided with an assist openings and is positioned at its uppermost component.
4. vegetal alga as claimed in claim 1 and microbe photosynthetic response system is characterized in that, this pressure transfusion unit is a pressure transfusion pump.
5. vegetal alga as claimed in claim 1 and microbe photosynthetic response system is characterized in that, this liquid level regulation apparatus comprises exntension tubs and this adjusting tube of winding, and these exntension tubs are provided with a pressure regulation opening.
6. vegetal alga as claimed in claim 1 and microbe photosynthetic response system, it is characterized in that, this deoxygenation and regulon comprise a communication apparatus, and this communication apparatus is connected in the bottom of this liquid cylinder and the bottom of this adjusting tube, and this communication apparatus also has a cleaning valve assembly.
7. vegetal alga as claimed in claim 1 and microbe photosynthetic response system is characterized in that, comprise the valve module of gathering, and this valve module of gathering is connected between the exit end and the unitary inlet end of this pressure transfusion of this printing opacity pipeline.
8. vegetal alga as claimed in claim 1 and microbe photosynthetic response system is characterized in that, further comprise a heating unit, and this heating unit is connected between the exit end and the unitary inlet end of this pressure transfusion of this printing opacity pipeline.
9. vegetal alga as claimed in claim 1 and microbe photosynthetic response system is characterized in that, further comprise a watering unit, and this watering unit is positioned at the unitary top of this photosynthetic response.
10. vegetal alga and microbe photosynthetic response method is characterized in that step comprises:
(1) provides a printing opacity pipeline, a pressure transfusion unit and a deoxygenation and regulon;
(2) inject a nutrient solution and algae kind in this printing opacity pipeline, it is interior to carry out photosynthesis and generation oxygen that this nutrient solution flows in this printing opacity pipeline, and this nutrient solution also flows to this pressure transfusion unit;
(3) open this pressure transfusion unit and flow to this deoxygenation and regulon, this nutrient solution is impacted in this deoxygenation and regulon splash shape to discharge oxygen to form a rotation spray diffusion to force this nutrient solution; And
(4) collect this nutrient solution in this deoxygenation and regulon, and aspirate this nutrient solution and flow in this printing opacity pipeline to carry out photosynthesis once more.
11. vegetal alga as claimed in claim 10 and microbe photosynthetic response method is characterized in that, the nutrient solution of this step (two) from top to bottom flows in this printing opacity pipeline in the mode of circulation in proper order.
12. vegetal alga as claimed in claim 10 and microbe photosynthetic response method is characterized in that this step (two) further provide a heating unit, this nutrient solution is flowed through behind this heating unit, flows to this pressure transfusion unit again.
13. vegetal alga as claimed in claim 10 and microbe photosynthetic response method is characterized in that, this step (two) further provides a watering unit, sprinkles water on this printing opacity pipeline in this watering unit.
14. vegetal alga as claimed in claim 10 and microbe photosynthetic response method is characterized in that, this step (four) provides the valve module of gathering, and this nutrient solution is flowed through behind this printing opacity pipeline, draws this nutrient solution by this valve module of gathering.
Priority Applications (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNB2004100857425A CN100404661C (en) | 2004-10-11 | 2004-10-11 | Vegetal alga, and system and method of microbe potosynthesis reaction |
| CN200420013760.8U CN2744690Y (en) | 2004-10-11 | 2004-10-11 | Plant algae and microorganism photosynthetic reactor |
Applications Claiming Priority (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNB2004100857425A CN100404661C (en) | 2004-10-11 | 2004-10-11 | Vegetal alga, and system and method of microbe potosynthesis reaction |
| CN200420013760.8U CN2744690Y (en) | 2004-10-11 | 2004-10-11 | Plant algae and microorganism photosynthetic reactor |
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| Publication Number | Publication Date |
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| CN1760358A CN1760358A (en) | 2006-04-19 |
| CN100404661C true CN100404661C (en) | 2008-07-23 |
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| CN200420013760.8U Expired - Fee Related CN2744690Y (en) | 2004-10-11 | 2004-10-11 | Plant algae and microorganism photosynthetic reactor |
| CNB2004100857425A Expired - Fee Related CN100404661C (en) | 2004-10-11 | 2004-10-11 | Vegetal alga, and system and method of microbe potosynthesis reaction |
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| CN200420013760.8U Expired - Fee Related CN2744690Y (en) | 2004-10-11 | 2004-10-11 | Plant algae and microorganism photosynthetic reactor |
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Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101988034B (en) * | 2009-08-05 | 2013-05-08 | 卢朝煇 | Industrialized culture method for alga and system thereof |
| CN103436431A (en) * | 2013-08-12 | 2013-12-11 | 福建师范大学 | Lossless frustule conveying system for sealed type photobioreactor |
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| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN2744690Y (en) * | 2004-10-11 | 2005-12-07 | 卢朝辉 | Plant algae and microorganism photosynthetic reactor |
| CN101033448B (en) * | 2006-03-09 | 2011-05-11 | 卢朝辉 | Photosynthetic reaction system for algae microorganism |
| JP2007319039A (en) * | 2006-05-30 | 2007-12-13 | Chao Hui Lu | Photosynthetic reaction system of alga microorganism |
| CN101353619B (en) * | 2007-07-27 | 2013-03-06 | 卢朝辉 | Algae microbe photosynthetic response system |
| 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 |
| CN113383065A (en) * | 2019-01-31 | 2021-09-10 | 克里斯蒂亚诺·加比亚蒂 | Photobioreactor for blue-green algae culture |
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|---|---|---|---|---|
| CN2234443Y (en) * | 1995-07-31 | 1996-09-04 | 缪坚人 | Spirulina photosynthesis reactor |
| CN1475558A (en) * | 2003-06-09 | 2004-02-18 | 缪坚人 | Photosynthesis bioreactor system for industrial production of micro algae |
| CN2744690Y (en) * | 2004-10-11 | 2005-12-07 | 卢朝辉 | Plant algae and microorganism photosynthetic reactor |
-
2004
- 2004-10-11 CN CN200420013760.8U patent/CN2744690Y/en not_active Expired - Fee Related
- 2004-10-11 CN CNB2004100857425A patent/CN100404661C/en not_active Expired - Fee Related
Patent Citations (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN2234443Y (en) * | 1995-07-31 | 1996-09-04 | 缪坚人 | Spirulina photosynthesis reactor |
| CN1475558A (en) * | 2003-06-09 | 2004-02-18 | 缪坚人 | Photosynthesis bioreactor system for industrial production of micro algae |
| CN2744690Y (en) * | 2004-10-11 | 2005-12-07 | 卢朝辉 | Plant algae and microorganism photosynthetic reactor |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101988034B (en) * | 2009-08-05 | 2013-05-08 | 卢朝煇 | Industrialized culture method for alga and system thereof |
| CN103436431A (en) * | 2013-08-12 | 2013-12-11 | 福建师范大学 | Lossless frustule conveying system for sealed type photobioreactor |
Also Published As
| Publication number | Publication date |
|---|---|
| CN1760358A (en) | 2006-04-19 |
| CN2744690Y (en) | 2005-12-07 |
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