CN204918572U - U type runway pond photobioreactor - Google Patents
U type runway pond photobioreactor Download PDFInfo
- Publication number
- CN204918572U CN204918572U CN201520474501.3U CN201520474501U CN204918572U CN 204918572 U CN204918572 U CN 204918572U CN 201520474501 U CN201520474501 U CN 201520474501U CN 204918572 U CN204918572 U CN 204918572U
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- raceway pond
- algae
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- shaped
- pond
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Abstract
The utility model discloses a U type runway pond photobioreactor, including: a U -shaped runway pond, be used for to for breeding little algae the gas supply system of runway pond air feed, be used for promoting algae liquid in the runway pond pushes away class system in the mobile variable speed of runway pond inner loop and gathers in the crops the system with the little algae that is used for collecting little algae. The utility model discloses a design of adopting U -shaped runway pond plus gas supply system, variable speed to push away a class system, little algae results system has been solved little algae effectively and has been attached wall phenomenon and algae liquid layering problem, has improved cultivation density and the productivity ratio of little algae.
Description
Technical field
The utility model relates to both culturing microalgae engineering field, particularly relates to a kind of U-shaped raceway pond bioreactor for both culturing microalgae.
Background technology
Micro-algae is a kind of photoautotroph, can absorbing carbon dioxide, utilize the organism such as inorganic salt synthetic protein, lipid acid, be with a wide range of applications in bio-pharmaceuticals, nutritious prod, healthcare products, bio-feritlizer, whole food processing, biological feed, sewage disposal and Energy production etc.The photosynthetic efficiency of micro-algae is high, can a large amount of production biomass at short notice, and along with the deterioration of the day by day exhausted of the worldwide petrochemical energy and environment, micro-algae is subject to extensive concern as a kind of potential biomass energy producer.
In order to improve the culture density of micro-algae, people devise many bioreactors, and according to the relation of algae liquid and external environment, bioreactor can be divided into open and closed two types.
The material manufacture that closed photo bioreactor entirety employs printing opacity good forms, adopt natural light or artificial light illumination, light can effectively enter in algae liquid, the mode amassing volume ratio to increase illuminating surface improves the optical energy utilization efficiency of micro-algae, has the advantages such as culture density is high, working condition is controlled.But in closed photo bioreactor, along with the growth of microalgae cell, micro-algae can form microbial film or the attached wall growth of micro-algae on the reactor wall that fluid velocity is less.The attached wall of micro-algae has greatly been decayed incident light intensity, causes bioreactor efficiency to reduce, therefore needs periodic cleaning, add cost and the complicacy of maintenance.In addition, existing closed photo bioreactor more or less easily causes the various problems such as dissolved oxygen accumulation, flow blind angle, equipment manufacturing cost costliness, cannot realize micro-algae low cost, pilot scale culture preferably.
Race-way photobioreactor has simple, easy to maintenance, the easy expansion scale of structure and the advantage such as cost is lower, directly utilizes the sun to produce.Particularly open raceway pond bioreactor, has been commonly used scale operation microalgae biomass.Current raceway pond reactor uses mechanical impellor to stir mostly, and the scope of turbulent closure scheme impact is also only limitted to the basin near impeller, and other region is laminar flow mostly, and algae liquid easily goes up lower leaf, and the problem such as the ratio that there is dead band is excessive.Although aeration at the bottom of pond improves the homogeneity of mixing, the only guarantee good mixing when the distribution density of aeration point is larger.In addition, Race-way photobioreactor is comparatively large due to volume, and generally all belongs to stationary installation, cannot move by easy removal once install.
Utility model content
The technical problems to be solved in the utility model is to provide a kind of U-shaped raceway pond bioreactor, and its energy consumption is low, culture density and productivity high, can be used for microalgae mass cultivate.
For solving the problems of the technologies described above, U-shaped raceway pond bioreactor of the present utility model, includes: for the U-shaped raceway pond of cultivating microalgae, for the airing system to described raceway pond air feed, for promoting the algae liquid in described raceway pond in the speed change plug-flow system of raceway pond internal circulation flow and the microalgae harvesting system for collecting micro-algae.
Described raceway pond bottom surface is arc surface, and the central angle of circular arc is 20 ~ 180 °; Raceway pond sidewall is two planes, and these two planes connect with circular arc respectively, and tangent with the circle at circular arc place; Described raceway pond sidewall offers the outlet of algae liquid.If desired, transparent cover plate or overlay can be covered in the upper surface sealing of described raceway pond.
Described airing system comprises aeration tube and air pump, and described aerator pipe frame is located at the mid-way bottom described raceway pond, and aeration tube is evenly distributed with solarization air cap, and described air pump is connected with aeration tube.
Described speed change plug-flow system comprises plug-flow pump, and described plug-flow pump bracket is located in raceway pond.
Described microalgae harvesting system includes micro-algae subsider and micro-algae receiving tank, and described micro-algae subsider takes the shape of the letter U, and bottom surface is arc surface, and this micro-algae subsider is connected with the sidewall of raceway pond; Described micro-algae receiving tank is connected to after described micro-algae subsider.
Described U-shaped raceway pond bioreactor can also include for supporting and the support of fixing raceway pond.Preferably, described support can be dismantled.
Compared with existing bioreactor, the U-shaped raceway pond bioreactor of packaged type of the present utility model, has the following advantages and beneficial effect:
1. raceway pond bottom surface of the present utility model is U-shaped structure, and during aeration, liquid-flow drives the flowing of algae liquid, algae liquid can be made to mix, improve the light utilising efficiency of micro-algae;
2. the utility model adopts the design of the additional airing system of U-shaped raceway pond, speed change plug-flow system, microalgae harvesting system, can effectively solve the attached wall phenomenon of micro-algae and algae liquid lamination problem with lower energy consumption;
3. if desired (when such as raining), with transparent cover plate or covered rearing with plastic film raceway pond of the present utility model, the environment of relative closure can be formed, effectively to reduce external pollution;
4. detachable bracket can be adopted to support and fix raceway pond, therefore dismounting and conveniently moving, can be used for the operation of a large amount of live body microalgae biomass of needs such as soil improvement, the micro-algae chemical fertilizers production of live body, realizes namely producing i.e. use, reduces the cost of transport and preservation algae liquid.
Accompanying drawing explanation
Fig. 1 is the vertical view of the U-shaped raceway pond bioreactor of packaged type of the present utility model;
Fig. 2 is the side-view of the U-shaped raceway pond bioreactor of packaged type of the present utility model.
In figure, description of reference numerals is as follows:
1: raceway pond
2: aeration tube
3: plug-flow pump
4: air pump
5: micro-algae subsider
6: micro-algae receiving tank
7: support
Embodiment
Understand more specifically for having technology contents of the present utility model, feature and effect, now by reference to the accompanying drawings, details are as follows:
As shown in Figure 1, 2, the U-shaped raceway pond bioreactor of packaged type of the present embodiment, includes: raceway pond 1, aeration tube 2, plug-flow pump 3, air pump 4, micro-algae subsider 5, micro-algae receiving tank 6 and support 7.
Raceway pond 1 is U-shaped, and bottom surface is arc surface, and the central angle of arc surface is 120 °, and raceway pond sidewall is two planes, and these two planes connect with circular arc respectively, and tangent with the circle at circular arc place.The upper surface sealing of raceway pond 1 is coated with transparent film.
Mid-way erection bottom raceway pond 1 has aeration tube 2, for raceway pond 1 inner homogeneous air feed.Aeration tube 2 is evenly distributed with the solarization air cap (figure does not draw) of diameter 2 millimeters, the external air pump 4 of aeration tube 2.
In raceway pond 1, erection has 2 plug-flow pumps 3, for driving algae liquid in raceway pond 1 at raceway pond 1 internal circulation flow.
The sidewall of raceway pond 1 offers the outlet of algae liquid.The external micro-algae subsider 5 of this algae liquid outlet, this micro-algae subsider takes the shape of the letter U, and bottom surface is arc surface.Micro-algae receiving tank 6 is connect after micro-algae subsider 5.Described micro-algae subsider 5 for receiving the algae liquid of discharging from raceway pond 1, and falls to after bottom micro-algae subsider 5 until micro-algae, and micro-algae is entered micro-algae receiving tank 6.Micro-algae that described micro-algae receiving tank 6 is discharged for collecting micro-algae subsider 5.
Support 7 adopts zinc-plated square tube to make, for supporting and fixing raceway pond 1.This support 7 is detachable, to facilitate the dismounting of bioreactor, assembling, movement.
The U-shaped raceway pond bioreactor of above-mentioned packaged type is when for both culturing microalgae, rise under buoyancy from aeration tube 2 bubble out, liquid is around driven to form one upwelling, algae liquid in raceway pond 1 Homogeneous phase mixing under the effect of this strand of upwelling, thus effectively prevent the attached wall phenomenon of micro-algae on raceway pond 1 surface.Meanwhile, plug-flow pump 3 drives the algae liquid in raceway pond 1 overall at raceway pond 1 internal recycle, which improves optical energy utilization efficiency and the culture density of microalgae cell.Because the sealing of raceway pond 1 upper surface is coated with transparent film, thus be formed as sealed raceway pond bioreactor, decrease the evaporation of moisture and the pollution of dust in air.During to microalgae harvesting, algae liquid is entered micro-algae subsider 5 from the algae liquid outlet of raceway pond 1, after micro-algae sedimentation, the more micro-algae fallen to bottom micro-algae subsider 5 is entered micro-algae receiving tank 6.
Claims (8)
1.U type raceway pond bioreactor, it is characterized in that, include: for the U-shaped raceway pond of cultivating microalgae, for the airing system to described raceway pond air feed, for promoting the algae liquid in described raceway pond in the speed change plug-flow system of raceway pond internal circulation flow and the microalgae harvesting system for collecting micro-algae.
2. U-shaped raceway pond bioreactor according to claim 1, is characterized in that, described raceway pond bottom surface is arc surface, and the central angle of circular arc is 20 ~ 180 °; Raceway pond sidewall is two planes, and these two planes connect with circular arc respectively, and tangent with the circle at circular arc place; Described raceway pond sidewall offers the outlet of algae liquid.
3. U-shaped raceway pond bioreactor according to claim 1 and 2, is characterized in that, the upper surface sealing of described raceway pond is coated with transparent cover plate or overlay.
4. U-shaped raceway pond bioreactor according to claim 1, it is characterized in that, described airing system comprises aeration tube and air pump, and described aerator pipe frame is located at the mid-way bottom described raceway pond, aeration tube is evenly distributed with solarization air cap, and described air pump is connected with described aeration tube.
5. U-shaped raceway pond bioreactor according to claim 1, is characterized in that, described speed change plug-flow system comprises plug-flow pump, and described plug-flow pump bracket is located in raceway pond.
6. U-shaped raceway pond bioreactor according to claim 1, it is characterized in that, described microalgae harvesting system includes micro-algae subsider and micro-algae receiving tank, and described micro-algae subsider takes the shape of the letter U, bottom surface is arc surface, and this micro-algae subsider is connected with the sidewall of raceway pond; Described micro-algae receiving tank is connected to after described micro-algae subsider.
7. U-shaped raceway pond bioreactor according to claim 1, is characterized in that, also includes for supporting and the support of fixing raceway pond.
8. U-shaped raceway pond bioreactor according to claim 7, it is characterized in that, described support can be dismantled.
Priority Applications (1)
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CN201520474501.3U CN204918572U (en) | 2015-06-30 | 2015-06-30 | U type runway pond photobioreactor |
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CN201520474501.3U CN204918572U (en) | 2015-06-30 | 2015-06-30 | U type runway pond photobioreactor |
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CN201520474501.3U Expired - Fee Related CN204918572U (en) | 2015-06-30 | 2015-06-30 | U type runway pond photobioreactor |
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Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN106544263A (en) * | 2016-11-02 | 2017-03-29 | 常德炎帝生物科技有限公司 | A kind of bioreactor and preparation method thereof |
CN107384801A (en) * | 2017-08-21 | 2017-11-24 | 李彤 | Closing biological membrane type cultural method for industrialized production microalgae |
CN107460129A (en) * | 2017-08-21 | 2017-12-12 | 李彤 | The industrialization microalgae culture method that biomass separates with nutrient solution |
CN110669638A (en) * | 2019-09-30 | 2020-01-10 | 宁波倍加福生物技术有限公司 | Microalgae breeding runway pool and working method thereof |
-
2015
- 2015-06-30 CN CN201520474501.3U patent/CN204918572U/en not_active Expired - Fee Related
Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN106544263A (en) * | 2016-11-02 | 2017-03-29 | 常德炎帝生物科技有限公司 | A kind of bioreactor and preparation method thereof |
CN107384801A (en) * | 2017-08-21 | 2017-11-24 | 李彤 | Closing biological membrane type cultural method for industrialized production microalgae |
CN107460129A (en) * | 2017-08-21 | 2017-12-12 | 李彤 | The industrialization microalgae culture method that biomass separates with nutrient solution |
CN110669638A (en) * | 2019-09-30 | 2020-01-10 | 宁波倍加福生物技术有限公司 | Microalgae breeding runway pool and working method thereof |
CN110669638B (en) * | 2019-09-30 | 2024-04-19 | 旭无线(宁波)智能卫浴有限公司 | Microalgae cultivation runway pool and working method thereof |
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C14 | Grant of patent or utility model | ||
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CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20151230 Termination date: 20210630 |
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CF01 | Termination of patent right due to non-payment of annual fee |