CN206188786U - Absorb little algae photobioreactor of carbon dioxide - Google Patents
Absorb little algae photobioreactor of carbon dioxide Download PDFInfo
- Publication number
- CN206188786U CN206188786U CN201621084395.9U CN201621084395U CN206188786U CN 206188786 U CN206188786 U CN 206188786U CN 201621084395 U CN201621084395 U CN 201621084395U CN 206188786 U CN206188786 U CN 206188786U
- Authority
- CN
- China
- Prior art keywords
- reactor
- carbon dioxide
- microalgae
- feed flow
- pipeline
- 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.)
- Active
Links
Landscapes
- Apparatus Associated With Microorganisms And Enzymes (AREA)
- Cultivation Of Seaweed (AREA)
Abstract
The utility model discloses an absorb little algae photobioreactor of carbon dioxide is mainly by supplying liquid bath (9), pipeline reactor (10) and liquid storage tank (11) to constitute, supply liquid bath (9) to supply the liquid bath for the closed type, and supply liquid bath (9) to be located little algae photobioreactor's upper portion, pipeline reactor (10) are the transparent coiled pipe, and pipeline reactor (10) are located little algae photobioreactor's middle part, liquid storage tank (11) are located little algae photobioreactor's lower part, supply liquid bath (9) lower part to pass through pipeline connection pipeline reactor (10) entry, pipeline reactor (10) export is through pipeline connection liquid storage tank (11) entry. Little algae photobioreactor can avoid little algae to receive external pollution, has avoided the destruction of circulating pump little algae in to algae liquid.
Description
Technical field
The utility model is related to microalgae photobiological reactor field, specifically refers to the reaction of absorbing carbon dioxide microalgae photobiological
Device.
Background technology
With the development of Microalgae biotechnology, Microalgae biotechnology has been widely used for all trades and professions, wherein important
Using being:The algae solution of microalgae biology, carbon dioxide and nutrient solution is loaded into container, container connection water pump, water pump connection culture
Device, water pump pumps into the algae solution in container in culture apparatus, and forms algae solution circulation, and culture apparatus is placed in the sun, micro-
Algae generates algae organic matter under photosynthesis, after promoting micro algae growth, micro algae growth to reach to a certain degree, will contain microalgae
Liquid centrifugal concentrating after as organic fertilizer or bait feed.
During being somebody's turn to do, container is open container, and the microalgae biology in algae solution is easily polluted by the external world, and algae solution is utilized
Water pump is circulated, and the microalgae biology in algae solution is easily destroyed.
Utility model content
The purpose of this utility model is to provide absorbing carbon dioxide microalgae photobiological reactor, microalgae photobiological reaction
Device is provided with enclosed and enters liquid pool, can prevent microalgae from being polluted by the external world, meanwhile, the microalgae photobiological reactor utilizes gravitational potential
Can circulate algae solution, it is to avoid the destruction of microalgae in algae solution.
The utility model is achieved through the following technical solutions:
Absorbing carbon dioxide microalgae photobiological reactor, is mainly made up of feed flow pond, pipeline reactor and liquid storage tank;It is described
Feed flow pond is closed type feed flow pond, enables the microalgae photobiological reactor to avoid microalgae from being polluted by the external world, and feed flow pond
Positioned at the top of microalgae photobiological reactor;The pipeline reactor is transparent coiled pipe, to increase illuminating area, and pipeline
Reactor is located at the middle part of microalgae photobiological reactor;The liquid storage tank is located at the bottom of microalgae photobiological reactor;The confession
Liquid pool bottom connects liquid storage tank entrance by pipeline connecting pipe reactor inlet, pipeline reactor outlet by pipeline.Feed flow
The top-down arrangement in position in pond, pipeline reactor and liquid storage tank three, can make the microalgae photobiological reactor be not required to carry
For recycle units such as pumps, only need to can circulate algae solution using gravitional force, it is to avoid destruction of the circulating pump to microalgae in algae solution.
Further, multiple carbon dioxide sensors, multiple material-feeding ports and multiple are provided with the pipeline reactor to go out
Material mouth, material-feeding port and discharging opening are both provided with switch.The titanium dioxide of carbon dioxide sensor real-time monitoring its position algae solution
Concentration of carbon, and by data reflection to display, if gas concentration lwevel is low, carbon dioxide is added by material-feeding port,
If adding carbon dioxide-depleted to finish, algae solution is discharged in liquid storage tank by discharging opening.
Further, the microalgae photobiological reactor is provided with many set of tubes reactors, many equal positions of set of tubes reactor
In feed flow pond lower section, and it is all located at liquid storage tank top.Many set of tubes reactors can simultaneously work and can also partly work, according to
Actual situation, if demand is small, the work of section of tubing reactor, if demand is big, whole pipeline reactors are all
Work.
Further, it is provided with adjustable throttling in the connecting pipeline between the feed flow pond and pipeline reactor.Microalgae
Absorption rate to carbon dioxide under different illumination conditions with condition of different temperatures is different, and when absorption rate is fast, regulation can
Flow regulating valve increases its flow, largely to utilize equipment;When absorption rate is slow, regulation adjustable throttling flows it
Amount reduces, with largely absorbing carbon dioxide.
Further, the microalgae photobiological reactor is provided with centrifuge, the first water pump, the second water pump and clear water reserviors,
The centrifuge liquid-feeding end connects liquid storage tank, and centrifuge clear water output end connection clear water reserviors, centrifuge separates the algae in liquid storage tank
Liquid, the microalgae and liquid in algae solution are separated, and microalgae enters clear water reserviors profit to be recycled as organic fertilizer or bait feed, liquid
With;The liquid feeding end connection liquid storage tank of first water pump, output end connection feed flow pond, the setting can be by the algae solution in liquid storage tank
In pumping into feed flow pond, using the microalgae in algae solution as feed flow pond algae kind;The liquid feeding end connection clear water reserviors of second water pump, it is defeated
Go out end connection feed flow pond, during the liquid in clear water reserviors can be pumped into feed flow pond by the setting, so that liquid circulation is utilized.
Further, the feed flow pond is provided with carbon dioxide mix device and nutrient solution adding apparatus, to match somebody with somebody on demand
Put the concentration of microalgae, carbon dioxide and nutrient solution.
The utility model compared with prior art, have the advantage that for:
(1) the utility model can avoid microalgae from being polluted by the external world, it is to avoid circulating pump breaks to microalgae in algae solution
It is bad.
(2) the utility model can be according to actual conditions real-time regulation flow, real-time feed supplement, real-time blowing, you can maximum
The utilization equipment of limit, can make that carbon dioxide absorption is more complete again, and production efficiency is high.
(3) algae kind of the present utility model and liquid circulation are utilized, cost-effective.
Brief description of the drawings
Fig. 1 is the structural representation of the utility model embodiment 1.
Fig. 2 is the structural representation of the utility model embodiment 2.
Wherein:1- clear water reserviors, 2- centrifuges, the water pumps of 3- second, the water pumps of 4- first, 5- adjustable throttlings, 6- material-feeding ports, 7-
Discharging opening, 8- carbon dioxide sensors, 9- feed flows pond, 10- pipeline reactors, 11- liquid storage tanks.
Specific embodiment
The utility model is described in further detail with reference to embodiment, but implementation method of the present utility model is not
It is limited to this.
Embodiment 1:
As shown in figure 1, the utility model is in order to overcome the defect of prior art, there is provided absorbing carbon dioxide microalgae photoproduction
Thing reactor.The microalgae photobiological reactor is mainly made up of feed flow pond 9, pipeline reactor 10 and liquid storage tank 11;The confession
Liquid pool 9 is closed type feed flow pond 9, enables the microalgae photobiological reactor to avoid microalgae from being polluted by the external world, and feed flow pond 9
Positioned at the top of microalgae photobiological reactor;The pipeline reactor 10 is transparent coiled pipe, to increase illuminating area, and pipe
Road reactor 10 is located at the middle part of microalgae photobiological reactor;The liquid storage tank 11 is located at the bottom of microalgae photobiological reactor;
The bottom of feed flow pond 9 exports and connects liquid storage by pipeline by the entrance of pipeline connecting pipe reactor 10, pipeline reactor 10
The entrance of pond 11.The top-down arrangement in position in feed flow pond 9, pipeline reactor 10 and the three of liquid storage tank 11, can make the microalgae
Bioreactor is not required to provide the recycle unit such as pump, only need to can circulate algae solution using gravitional force, it is to avoid circulating pump
Destruction to microalgae in algae solution.
In feed flow pond 9, the algae solution containing algae kind, carbon dioxide and nutrient solution is configured, effect of the algae solution in gravity
In lower entrance pipeline reactor 10, and illumination is received in pipeline reactor 10, absorb the carbon dioxide in algae solution, photosynthesis
Produce algae organic matter, algae organic matter promote micro algae growth, micro algae growth to a certain extent after, liquid gravity you use under
Flow into liquid storage tank 11.
Embodiment 2:
The present embodiment is further improved on the basis of embodiment 1, as shown in Fig. 2 being set in the pipeline reactor 10
Multiple carbon dioxide sensors 8, multiple material-feeding ports 6 and multiple discharging openings 7 are equipped with, material-feeding port 6 and discharging opening 7 are both provided with out
Close.The gas concentration lwevel of the real-time monitoring of carbon dioxide sensor 8 its position algae solution, and by data reflection to display
In, if gas concentration lwevel is low, carbon dioxide is added by material-feeding port 6, if adding carbon dioxide-depleted to finish, lead to
Cross discharging opening 7 algae solution is discharged in liquid storage tank 11.
The microalgae photobiological reactor is provided with many set of tubes reactors 10, and many set of tubes reactors 10 are respectively positioned on feed flow
The lower section of pond 9, and it is all located at the top of liquid storage tank 11.Many set of tubes reactors 10 can simultaneously work and can also partly work, according to
Actual situation, if demand is small, section of tubing reactor 10 works, if demand is big, whole pipeline reactors
10 all work.
Adjustable throttling 5 is provided with connecting pipeline between the feed flow pond 9 and pipeline reactor 10.Microalgae is in difference
Illumination condition is different with the absorption rate under condition of different temperatures to carbon dioxide, when absorption rate is fast, adjusts adjustable throttling
Valve 5 increases its flow, largely to utilize equipment;When absorption rate is slow, regulation adjustable throttling 5 subtracts its flow
It is small, with largely absorbing carbon dioxide.
The microalgae photobiological reactor is provided with centrifuge 2, the first water pump 4, the second water pump 3 and clear water reserviors 1, it is described from
The liquid feeding end of scheming 2 connects liquid storage tank 11, and the clear water output end of centrifuge 2 connection clear water reserviors 1, centrifuge 2 is separated in liquid storage tank 11
Algae solution, the microalgae and liquid in algae solution are separated, and microalgae is waited to follow as organic fertilizer or bait feed, liquid into clear water reserviors 1
Ring is utilized;The liquid feeding end connection liquid storage tank 11 of first water pump 4, output end connection feed flow pond 9, the setting can be by liquid storage tank
Algae solution in 11 is pumped into feed flow pond 9, using the microalgae in algae solution as feed flow pond 9 algae kind;The liquid feeding end of second water pump 3
Connection clear water reserviors 1, output end connection feed flow pond 9, during the liquid in clear water reserviors 1 can be pumped into feed flow pond 9 by the setting, so that liquid
Body circulation is utilized.
The feed flow pond 9 is provided with carbon dioxide mix device and nutrient solution adding apparatus, to configure microalgae, two on demand
The concentration of carbonoxide and nutrient solution.
The other parts of the present embodiment are same as Example 1, repeat no more.
The above, is only preferred embodiment of the present utility model, and any formal limit is not done to the utility model
System, every any simple modification, equivalent variations made to above example according to technical spirit of the present utility model each fall within
Within protection domain of the present utility model.
Claims (6)
1. absorbing carbon dioxide microalgae photobiological reactor, it is characterised in that:The microalgae photobiological reactor is main by feed flow
Pond (9), pipeline reactor (10) and liquid storage tank (11) composition;The feed flow pond (9) is closed type feed flow pond, and feed flow pond (9)
Positioned at the top of microalgae photobiological reactor;The pipeline reactor (10) is transparent coiled pipe, and pipeline reactor (10)
Positioned at the middle part of microalgae photobiological reactor;The liquid storage tank (11) is positioned at the bottom of microalgae photobiological reactor;The feed flow
Pond (9) bottom connects liquid storage tank by pipeline connecting pipe reactor (10) entrance, pipeline reactor (10) outlet by pipeline
(11) entrance.
2. absorbing carbon dioxide microalgae photobiological reactor according to claim 1, it is characterised in that:The pipe reaction
Be provided with multiple carbon dioxide sensors (8), multiple material-feeding port (6) and multiple discharging opening (7) in device (10), material-feeding port (6) and
Discharging opening (7) is both provided with switch.
3. absorbing carbon dioxide microalgae photobiological reactor according to claim 1, it is characterised in that:The microalgae photoproduction
Thing reactor is provided with many set of tubes reactors (10), and many set of tubes reactors (10) are respectively positioned on feed flow pond (9) lower section, and all positions
In liquid storage tank (11) top.
4. absorbing carbon dioxide microalgae photobiological reactor according to claim 1, it is characterised in that:The feed flow pond
(9) adjustable throttling (5) is provided with the connecting pipeline and between pipeline reactor (10).
5. absorbing carbon dioxide microalgae photobiological reactor according to claim 1, it is characterised in that:The microalgae photoproduction
Thing reactor is provided with centrifuge (2), the first water pump (4), the second water pump (3) and clear water reserviors (1), centrifuge (2) feed liquor
End connection liquid storage tank (11), centrifuge (2) clear water output end connects clear water reserviors (1);The liquid feeding end connection of first water pump (4)
Liquid storage tank (11), output end connects feed flow pond (9);The liquid feeding end of second water pump (3) connects clear water reserviors (1), and output end connects
Connect feed flow pond (9).
6. absorbing carbon dioxide microalgae photobiological reactor according to claim 1, it is characterised in that:The feed flow pond
(9) carbon dioxide mix device and nutrient solution adding apparatus are provided with.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201621084395.9U CN206188786U (en) | 2016-09-24 | 2016-09-24 | Absorb little algae photobioreactor of carbon dioxide |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201621084395.9U CN206188786U (en) | 2016-09-24 | 2016-09-24 | Absorb little algae photobioreactor of carbon dioxide |
Publications (1)
Publication Number | Publication Date |
---|---|
CN206188786U true CN206188786U (en) | 2017-05-24 |
Family
ID=58730493
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN201621084395.9U Active CN206188786U (en) | 2016-09-24 | 2016-09-24 | Absorb little algae photobioreactor of carbon dioxide |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN206188786U (en) |
-
2016
- 2016-09-24 CN CN201621084395.9U patent/CN206188786U/en active Active
Similar Documents
Publication | Publication Date | Title |
---|---|---|
Carvalho et al. | Microalgal reactors: a review of enclosed system designs and performances | |
CN101985595B (en) | Membrane type photobioreactor for enhancing microalgae culturing | |
JP2019141056A (en) | Large scale mixotrophic production systems | |
CN103476245B (en) | For cultivating the method for microorganism and bioreactor | |
CN105255731B (en) | Circumfusion formula cell culture system and bioreactor thereof | |
CN101899394B (en) | External circulation animal cell culture bioreactor | |
WO2020085366A1 (en) | Gas dissolving device and algae cultivation device | |
CA2826345A1 (en) | Light energy supply for photobioreactor system | |
CN206188786U (en) | Absorb little algae photobioreactor of carbon dioxide | |
CN206887129U (en) | Disposable pneumo lift-type cell culture reactor | |
CN106281974A (en) | A kind of oil-producing microalgae culture apparatus and cultural method thereof | |
CN203238266U (en) | Photobioreactor device for culturing microalgae in high density | |
CN207891126U (en) | A kind of jetting type IC anaerobic reactors | |
CN201241156Y (en) | Toxin production algae light biological reaction apparatus | |
CN107557290B (en) | Continuous culture apparatus for micro algae | |
CN206843447U (en) | A kind of gravity flow photosynthetic reaction device | |
CN109251847A (en) | Utilize the device and method of sunlight culture photosynthetic microorganism | |
CN101613661A (en) | Buffering/collecting system of optical bioreactor | |
CN201770705U (en) | Outer circulation bioreactor for animal cell culture | |
CN203238251U (en) | Microalgae culture pond with novel aeration device | |
CN202157065U (en) | Continuous culture device for plankton | |
CN205576120U (en) | Modular photobioreactor | |
CN106282006B (en) | A kind of automation equipment preserved for oceanic generator | |
CN105602837A (en) | Methanol protein airlift type external fermentation tank | |
CN218507804U (en) | Novel paddle-free stirring perfusion bioreactor |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
GR01 | Patent grant | ||
GR01 | Patent grant |