CN104031822A - Bionic laminated microalgae photosynthetic reactor - Google Patents
Bionic laminated microalgae photosynthetic reactor Download PDFInfo
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- CN104031822A CN104031822A CN201410271696.1A CN201410271696A CN104031822A CN 104031822 A CN104031822 A CN 104031822A CN 201410271696 A CN201410271696 A CN 201410271696A CN 104031822 A CN104031822 A CN 104031822A
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- C12M29/00—Means for introduction, extraction or recirculation of materials, e.g. pumps
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Abstract
The invention discloses a bionic laminated microalgae photosynthetic reactor. A submersible pump is arranged at the bottom of a microalgae culture liquid storage tank and is connected with water feeding distribution pipes which are uniformly distributed on the top of a tower main body angle steel bracket through a main suction tube; a photosynthetic reactor liquid storage tank is fixed on the tower main body angle steel bracket through a liquid storage tank angle steel bracket; the liquid storage tank angle steel bracket in the photosynthetic reactor liquid storage tank and the tower main body angle steel bracket form a triangular cuboid; a stainless steel wire mesh is fixed in the triangular cuboid formed by the liquid storage tank angle steel bracket and the tower main body angle steel bracket; a transparent plastic film is fixed on the inner side of the stainless steel wire mesh; a transparent corrugated plastic drainage plate is fixed on the outer side of the stainless steel wire mesh; the upper edge of the transparent corrugated plastic drainage plate is slightly higher than the upper edge of the stainless steel wire mesh; and the whole reactor consists of multiple photosynthetic reactor liquid storage tanks from a smaller size to a larger size from top to bottom. The bionic laminated microalgae photosynthetic reactor has the characteristics of high photosynthetic efficiency, energy conservation, high efficiency and convenience in maintenance and can realize economic large-scale continuous microalgae cultivation.
Description
Technical field
The present invention relates to a kind of for cultivating the biomimetic type laminated type photosynthetic organism reactor of micro-algae.
Background technology
Under the backgrounds of fossil oil exhaustion day by day, a large amount of discharges of greenhouse gases, exploitation renewable energy source, carries out energy-saving and emission-reduction, develops a circular economy and becomes increasingly important at present.Micro-algae, as a kind of novel biofuel, can effectively utilize CO
2carry out photosynthesis, be more and more subject to people's attention, simultaneously micro-algae is with a wide range of applications in food, feed, medicine, the many aspects such as purify waste water.
Along with deepening continuously of micro-algae research, people recognize gradually, and bioreactor is an important factor of the micro-algae high-density high-efficient culture of restriction, and the new and effective bioreactor of development has become one of gordian technique of Microalgae biotechnology industrialization.
At present, the bioreactor that micro-algae is cultivated mainly divides two kinds of open and closeds.The advantage of open reactive device be build simple, with low cost and simple to operate, shortcoming also clearly: (1) reactor floor space is large, and land utilization ratio is low; (2) illumination surface to volume ratio is low, and micro-algae photosynthetic efficiency is not high; (3) adopt mechanical stirring to promote the exchanges of mass and energy in culture, large (4) the open microalgae photobiological reactor of energy consumption is generally built on the ground, and surface water, animal, dry branches and fallen leaves damage ratio are more serious.
Although closed photo bioreactor has overcome the shortcoming of the open algae photosynthetic reactor that declines to a certain extent, but also there is serious deficiency: the cost compare of (1) reactor is high, operational requirement is also high, the operation and maintenance costs such as cleaning are very high, become the bottleneck problem of Closed photobioreactor commercial application; (2) oxygen easily occurs in closed reactor and pile up, can produce toxic action to the growth of micro-algae, this is the common fault of closed reactor; (3), in the time that the concentration of algae in reactor is higher, the light transmission variation of closed reactor, has affected light efficiency.
Summary of the invention
The object of the invention is to propose a kind of biomimetic type lamination algae photosynthetic reactor that declines, can increase substantially micro-algae output, efficiently carbon admittedly, low cost, convenient operation, safety coefficient are high.
The present invention is achieved by the following technical solutions.
The present invention is made up of micro-algae culture liquid storage tank (1), submersible pump (2), main body tail pipe (3), turriform main body angle bar frame (4), photosynthetic reactor reservoir (5), upper water distribution (9).
At the bottom of submersible pump (2) is placed in micro-algae culture liquid storage tank (1) pond, and be connected with turriform main body angle bar frame (4) the equally distributed upper water distribution in top (9) by main body tail pipe (3), photosynthetic reactor reservoir (5) is fixed on turriform main body angle bar frame (4) by reservoir angle bar frame (10).
Described photosynthetic reactor reservoir (5) is made up of lightweight transparent plastic film (6), Stainless Steel Cloth (7), transparent corrugation plastic drainage plate (8), reservoir angle bar frame (10); Reservoir angle bar frame (10) and turriform main body angle bar frame (4) composition triangle rectangular parallelepiped, Stainless Steel Cloth (7) is fixed on reservoir angle bar frame (10) and forms in triangle rectangular parallelepiped with turriform main body angle bar frame (4), transparent plastic film (6) is fixed on Stainless Steel Cloth (7) inner side, transparent corrugation plastic drainage plate (8) is fixed on the outside of Stainless Steel Cloth (7), and transparent corrugation plastic drainage plate (8) upper limb is a little more than the upper limb of Stainless Steel Cloth (7).Whole reactor is made up of some ascending photosynthetic reactor reservoirs (5) from top to bottom.
Principle of work of the present invention is: the micro-algae culture in micro-algae culture liquid storage tank (1) is pumped into and is positioned at turriform main body angle bar frame (4) the equally distributed upper water distribution in top (9) by main body tail pipe (3) with submersible pump (2), evenly spread in the photosynthetic reactor reservoir (5) of top, nutrient solution overflows rear dependence segregation drive and flows in lower one deck photosynthetic reactor reservoir along transparent corrugation plastic drainage plate (8), micro-algae culture is descending step by step in this way, until flow to the micro-algae culture of lowermost end liquid storage tank (1), form algae liquid exploitation formula circulation loop.
The present invention can also be by increasing the input aperture of a fresh micro-algae culture medium at main body tail pipe (3), and increase a culture outlet at micro-algae culture liquid storage tank (1), make fresh culture thing inlet and micro-algae culture discharge balance, realize continuously and producing.
The quantity of photosynthetic reactor reservoir of the present invention (5) can increase and decrease according to need of production.
The inclination angle of the Stainless Steel Cloth (7) of photosynthetic reactor reservoir of the present invention (5) can be adjusted apart from the variation of the solar incident angle of floor level and Various Seasonal according to each lamination, makes sunlight light as far as possible evenly incide each position of reactor.
Length in the horizontal direction of turriform main body angle bar frame, can be according to need of production adjustment.
The present invention has following technique effect: the biological structure feature of the overall imitation arbor of reactor, be shaped as laminated type pyramidal structure, and do not block mutually between layers, can accept the most fully solar irradiation, carry out photosynthesis, reach efficient carbon object admittedly.Whole framework is multiple trilaterals and connects, and layer angle of inclination is adjustable arbitrarily, in the situation that making full use of luminous energy, keeps the stability of whole system; The whole frame material of reactor is stainless steel, and it is meshy steel wire structure that interlayer is lifted material, and light transmission is good, and reactor body is selected lightweight transparent plastics, utilizes meshy steel wire structure to fix, and has solved that glass reaction is thought highly of and the shortcoming such as danger coefficient height; The flow pattern of reactor has adopted overflow mode, layer by layer, have transparent drainage baffle plate, algae liquid flows to lower floor bottom along drainage baffle plate under segregation drive, increases and stirs, be conducive to contacting of algae and outside air, effectively reduce the phenomenon of the adherent growth of algae.Therefore there is photosynthetic efficiency high, efficient energy-saving, feature easy to maintenance, is the good equipment of realizing economic micro-algae large-scale continous way cultivation.
Brief description of the drawings
Fig. 1 is the front view of schematic diagram of the present invention.
Fig. 2 is the side-view of schematic diagram of the present invention.
Fig. 3 is the partial enlarged drawing of the photosynthetic reactor reservoir 5 described in Fig. 1.
Wherein, 1 is micro-algae culture liquid storage tank, and 2 is submersible pump, and 3 is main body tail pipe, 4 is turriform main body angle bar frame, and 5 is photosynthetic reactor reservoir, and 6 is lightweight transparent plastic film, and 7 is Stainless Steel Cloth, 8 is transparent corrugation plastic drainage plate, and 9 is upper water distribution, and 10 is reservoir angle bar frame.
Embodiment
The present invention, in connection with accompanying drawing, is described further by following examples.
As shown in Figure of description, according to the target of processing 1 ton of natural pond liquid every day, the biomimetic type laminated type photosynthetic organism reactor number of plies is 5 layers, reactor level direction length is 10 meters, and the triangle space being supported at Stainless Steel Cloth 7 by lightweight transparent plastic film 6 is that the cubic capacity of photosynthetic reactor reservoir 5 is 10 cubic metres.First in micro-algae culture liquid storage tank, inject chlorella BG11 substratum 8000L, and the Chlorella vulgaris nutrient solution of pure culture (algae liquid biomass content is 4.3g/L) 2000L, start submersible pump, make algae liquid Cyclic culture in reactor, as 30 DEG C of culture temperature, light intensity 15,000Lux, cultured continuously 4 days, algae liquid biomass content is 1.3g/L.Within the 5th day, start the input aperture by increase a fresh micro-algae culture medium at main body tail pipe 3, deliver for sale the pretreated natural pond liquid storage pool of half congealed the set up natural pond liquid biomembrane filter tower of pig manure urine natural pond liquid that large-scale cultivation enterprise that live pig is 30,000 builds from being close to one, in photosynthetic reactor, supplement fresh natural pond liquid according to the speed of inputting 1 ton of natural pond liquid every day; Increase a culture outlet at micro-algae culture liquid storage tank 1 simultaneously, equally by the outwards micro-algae culture of output of the speed of 1 ton every day, make inlet and micro-algae culture discharge balance of fresh culture, realize continuously and producing.Micro-algae culture is sent into the continuous harvesting system of micro-algae, more than micro-algal biomass content wherein reaches 1.1g/L.
In order to expand the processing power of natural pond liquid, can increase the group number of the photosynthetic reactor of above-mentioned scale, and guarantee the stability of whole system operation by mode in parallel.
Claims (5)
1. the biomimetic type lamination algae photosynthetic reactor that declines, is characterized in that being made up of micro-algae culture liquid storage tank (1), submersible pump (2), main body tail pipe (3), turriform main body angle bar frame (4), photosynthetic reactor reservoir (5), upper water distribution (9);
At the bottom of submersible pump (2) is placed in micro-algae culture liquid storage tank (1) pond, and be connected with turriform main body angle bar frame (4) the equally distributed upper water distribution in top (9) by main body tail pipe (3), photosynthetic reactor reservoir (5) is fixed on turriform main body angle bar frame (4) by reservoir angle bar frame (10);
Described photosynthetic reactor reservoir (5) is made up of lightweight transparent plastic film (6), Stainless Steel Cloth (7), transparent corrugation plastic drainage plate (8), reservoir angle bar frame (10); Reservoir angle bar frame (10) and turriform main body angle bar frame (4) composition triangle rectangular parallelepiped, Stainless Steel Cloth (7) is fixed on reservoir angle bar frame (10) and forms in triangle rectangular parallelepiped with turriform main body angle bar frame (4), transparent plastic film (6) is fixed on Stainless Steel Cloth (7) inner side, transparent corrugation plastic drainage plate (8) is fixed on the outside of Stainless Steel Cloth (7), and transparent corrugation plastic drainage plate (8) upper limb is a little more than the upper limb of Stainless Steel Cloth (7); Whole reactor is made up of some ascending photosynthetic reactor reservoirs (5) from top to bottom.
2. the biomimetic type lamination according to claim 1 algae photosynthetic reactor that declines, is characterized in that increasing at main body tail pipe (3) input aperture of a fresh micro-algae culture medium, and increases a culture outlet at micro-algae culture liquid storage tank (1).
3. the biomimetic type lamination according to claim 1 algae photosynthetic reactor that declines, is characterized in that the quantity of described photosynthetic reactor reservoir (5) increases and decreases according to need of production.
4. the biomimetic type lamination according to claim 1 algae photosynthetic reactor that declines, is characterized in that the inclination angle of the Stainless Steel Cloth (7) of described photosynthetic reactor reservoir (5) is adjusted apart from the variation of the solar incident angle of floor level and Various Seasonal according to each lamination.
5. the biomimetic type lamination according to claim 1 algae photosynthetic reactor that declines, is characterized in that length in the horizontal direction of turriform main body angle bar frame is according to need of production adjustment.
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| CN201410271696.1A CN104031822B (en) | 2014-06-18 | 2014-06-18 | A kind of biomimetic type lamination declines algae photosynthetic reactor |
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Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106467888A (en) * | 2015-08-14 | 2017-03-01 | 国家开发投资公司 | Grated plate type bioreactor |
| CN106906119A (en) * | 2015-12-23 | 2017-06-30 | 国家开发投资公司 | The harvesting apparatus of bioreactor, harvesting method and photo-biological culture systems |
Families Citing this family (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108034567A (en) * | 2018-01-25 | 2018-05-15 | 浙江大学 | Lantern pipe ring fluidization tower declines algae photosynthetic reactor and the method for both culturing microalgae |
Citations (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH08140662A (en) * | 1994-11-22 | 1996-06-04 | Mitsui Eng & Shipbuild Co Ltd | Culture of fine algae in high concentration by utilization of deep layer water and device therefor |
| CN101693871A (en) * | 2009-09-30 | 2010-04-14 | 张炳泉 | Large-capacity multi-level energy-saving microalgae culturing method and device thereof |
| US20100216218A1 (en) * | 2009-02-26 | 2010-08-26 | Mei-Hua Huang | Apparatus for carbon dioxide-capture system and use of the same |
| CN102224236A (en) * | 2008-11-12 | 2011-10-19 | 拉曼大学教育基金会 | A photobioreactor |
| CN102618434A (en) * | 2012-02-17 | 2012-08-01 | 农业部规划设计研究院 | High-efficiency microalgae culturing device based on plant bionics |
| CN203904335U (en) * | 2014-06-18 | 2014-10-29 | 南昌大学 | Bionic laminated microalga photosynthesis reactor |
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2014
- 2014-06-18 CN CN201410271696.1A patent/CN104031822B/en not_active Expired - Fee Related
Patent Citations (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH08140662A (en) * | 1994-11-22 | 1996-06-04 | Mitsui Eng & Shipbuild Co Ltd | Culture of fine algae in high concentration by utilization of deep layer water and device therefor |
| CN102224236A (en) * | 2008-11-12 | 2011-10-19 | 拉曼大学教育基金会 | A photobioreactor |
| US20100216218A1 (en) * | 2009-02-26 | 2010-08-26 | Mei-Hua Huang | Apparatus for carbon dioxide-capture system and use of the same |
| CN101693871A (en) * | 2009-09-30 | 2010-04-14 | 张炳泉 | Large-capacity multi-level energy-saving microalgae culturing method and device thereof |
| CN102618434A (en) * | 2012-02-17 | 2012-08-01 | 农业部规划设计研究院 | High-efficiency microalgae culturing device based on plant bionics |
| CN203904335U (en) * | 2014-06-18 | 2014-10-29 | 南昌大学 | Bionic laminated microalga photosynthesis reactor |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106467888A (en) * | 2015-08-14 | 2017-03-01 | 国家开发投资公司 | Grated plate type bioreactor |
| CN106906119A (en) * | 2015-12-23 | 2017-06-30 | 国家开发投资公司 | The harvesting apparatus of bioreactor, harvesting method and photo-biological culture systems |
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