CN202297574U - Shower type photo-bioreactor - Google Patents
Shower type photo-bioreactor Download PDFInfo
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- CN202297574U CN202297574U CN 201120319664 CN201120319664U CN202297574U CN 202297574 U CN202297574 U CN 202297574U CN 201120319664 CN201120319664 CN 201120319664 CN 201120319664 U CN201120319664 U CN 201120319664U CN 202297574 U CN202297574 U CN 202297574U
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- 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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- 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
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- C12M23/04—Flat or tray type, drawers
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Abstract
The utility model discloses a shower type photo-bioreactor, which comprises a flat plate type photo-bioreactor, an alga solution shower unit, an industrial waste gas preprocessing unit and an alga solution circulating system, wherein the alga solution shower unit is arranged above the flat plate type photo-bioreactor; the industrial waste gas preprocessing unit is connected to the flat plate type photo-bioreactor; the alga solution circulating system is used for driving alga solution to circulate between the flat plate type photo-bioreactor and the alga solution shower unit; the alga solution shower unit comprises a shower device and a transparent curtain wall; the shower device is used for dispersing and flowing down the alga solution; and the transparent curtain wall is used for preventing the alga solution from spitting and preventing the alga solution from being in contact with the external environment. According to the technical scheme of the novel shower type photo-bioreactor provided by the utility model, high-density culture of the alga solution and high-efficiency absorption of carbon dioxide in industrial waste gas can be realized.
Description
Technical field
The utility model relates to bioreactor, particularly a kind of spray-type bioreactor.
Background technology
In recent years, climate warming has received the extensive concern in the whole world, and its major cause is the rising of carbonic acid gas isothermal chamber gas concentration in the atmosphere.Add up according to ICPP (Intergovernmental Panel on Climate Change of United Nations); Atmospheric Carbon Dioxide concentration rises to 0.036% by 0.028% before the Industrial Revolution; The rising of gas concentration lwevel can cause a series of environmental problems such as sea level rise, flooding of rivers, ecosystem distribution change, serious threat human existence.Industrial gaseous waste is the main source of carbonic acid gas in the atmosphere; With the fossil fired power plant is example; The scale of common fossil fired power plant is between 400-1200MW, and the electric energy of the every generation 1MWH of power plant will discharge the 344-941kg carbonic acid gas; Calculate like this, every year will be discharged number with 10,000,000,000 tons carbonic acid gas by global power plant.
Countries in the world are actively with regard to the seizure of carbonic acid gas with seal technology (CCS) up for safekeeping and launch research, and in numerous CCS, little algae carbon-fixation-technology receives increasing concern.Utilize little algae stabilizing carbon dioxide to have many advantages: (1) little algae can directly utilize sun power to carry out photosynthetic carbon fixation, and is energy-conservation than physico-chemical process; (2) little algal biomass can be applied to fields such as food, biomedicine, bio-feritlizer and renewable energy source, has important economy and social value; (3) little algae can be cultured on the barren soil, reduces the pressure to ploughing; (4) can combine with wastewater treatment, effectively remove in the water body nitrogen phosphorus etc. in the time of culturing microalgae.The domestic and international at present research for little algae stabilizing carbon dioxide mainly concentrates on following two aspects: (1) screens and incubation growth speed is fast, can tolerate high concentration CO
2, SO
x, NO
xAlgae kind Deng pollutent; (2) research and development of high-efficiency photobioreactor.The seed selection of good algae strain is no doubt important, but will be in actual application, and the good algae strain that seed selection is obtained obtains CO efficiently
2Fixed effect, the bioreactor of superior performance is absolutely necessary.
U.S. green energy resource technology company and the State of Arizona, US Public services subordinate's of company red hawk power plant cooperates; Successfully utilize stack gas to carry out little algae large scale culturing; And inverting biological fuel, the culture apparatus that the said firm adopts is the pillar bioreactor.Hawaiian blue-green algae biotech company supplies 67 runway ponds uses with the carbonic acid gas that small power plant produces with electric energy, can fix 67 tons of carbonic acid gas in every month, produces 36 tons of spirulina powders." solid carbon of the tower biology of industrial discharge carbon dioxide source and energy gordian technique pilot scale research " (University Of Science and Technology Of Shandong; 2009) pass through the evaluation of Shandong Province Science and Technology Department, and propose tower bio-reactor first, can three-dimensionally arrange; Floor space is little; Help to dissolve the carbon deoxidation, and less to the shearing action of frond, little algae continuous production.
At present domestic only have one piece of bioreactor patent to relate to the carbon fixation of little algae.Chai Xiaoli (Chinese utility model; CN102008930A; The photo-biological reactor that removes carbonic acid gas in flue gas 2011-04-13) is made up of optical-biological reaction system and on-line detecting system, and wherein the optical-biological reaction system is by bioreactor; And connected temperature regulating device, circulation device, air feeder and illumination apparatus composition, on-line monitoring system comprises temp probe, DO combined electrode, carbon dioxide electrode and pH electrode.This utility model has advantages such as the mass transfer effect of mixing is good, and shearing force is little, and the living weight rate of growth is fast, and co 2 removal is effective.
In theory, traditional bioreactor all can be used for the cultivation of the little algae of solid carbon.But consider the fixed efficiency of carbonic acid gas and the construction cost of reactor assembly, the relative limitation that alternative type of reactor becomes.In numerous type of reactor, CO
2The higher bioreactor of clearance has duct type and pillar, but duct type bioreactor oxygen is resolved difficulty of difficulty, difficult cleaning, cost height, temperature control; The pillar bioreactor does not exist oxygen to resolve and mixed problem, but its volume of culture is less, be difficult for amplifying (vertically with radially), specific surface area is little and reactor center light is difficult for penetrating, and production efficiency is low, all influences the solid carbon efficiencies of little algae.
At present, scientific research institution and enterprise generally adopt traditional bait micro-algae to cultivate the research that used bioreactor (runway pond, pillar, fermentation pot type, tubular type and suspended bag type) carries out the solid carbon of little algae, and there are many shortcomings technically in it:
(1) traditional bait micro-algae bioreactor be not for little algae efficiently admittedly carbon make up, its carbonic acid gas remove the theoretical speed of speed far below the solid carbon of little algae, need improve to its structure, can be used for production and research that little algae is consolidated carbon;
(2) efficiency of light energy utilization of little algae in traditional bioreactor is lower, and along with the increase of algae cell density, the effect of blocking between the cell is more obvious, has a strong impact on the growth of little algae and the absorption of carbonic acid gas;
(3) traditional bioreactor generally adopts the mode of bubbling to feed pressurized air, and the contact area of frustule and bubble is little, duration of contact is short, to a certain degree limit the uptake rate of frustule to carbonic acid gas;
(4) the temperature control poor effect of traditional bioreactor is only lowered the temperature through water-cooled or air-cooled mode, and energy consumption is huge;
(5) in order to increase the gas-liquid transfer efficiency, at reactor bottom hydrophobic aeration film is installed usually,, is stopped up, also can cause the increase of ventilation energy consumption but hydrophobic aeration film is easy to produce less and uniform bubble.
This shows that prior art all is difficult to realize the efficient fixing of carbonic acid gas, thereby is necessary to design a kind of novel bioreactor.
The utility model content
The purpose of the utility model is to provide a kind of spray-type bioreactor, in order to realize that the low-cost high-density efficient fixing and little algae of carbonic acid gas is cultivated in the industrial gaseous waste.
For solving above technical problem; The technical scheme that the utility model provides is; A kind of spray-type bioreactor; Comprise flat bioreactor, be arranged at the algae liquid spray unit of said flat bioreactor top, the industrial gaseous waste pretreatment unit that inserts said flat bioreactor and driving algae liquid round-robin algae fluid circulation between said flat bioreactor and said algae liquid spray unit; Wherein said algae liquid spray unit comprises: spray thrower, in order to algae liquid under the dispersion train; Transparent curtain wall is in order to prevent the splash of algae liquid and to stop algae liquid to contact with external environment.
More excellent ground, the transparent reaction container of said flat bioreactor for being bonded by some predetermined dimension transparent plates, the side of said transparent reaction container is equipped with ventpipe interface, outer circulating tube interface and prolong interface.
More excellent ground, said algae fluid circulation comprises: outer circulating tube is communicated with said flat bioreactor and said algae liquid spray unit; Recycle pump is positioned on the said outer circulating tube.
More excellent ground, said algae fluid circulation comprises: header tank, its fluid inlet and liquid outlet are communicated with said flat bioreactor and said algae liquid spray unit through outer circulating tube respectively; Source of the gas, its air feed port is connected on the riser culverts of said outer circulating tube.
More excellent ground, said transparent curtain wall is processed by transparent plastic film, and said transparent plastic film is covered on the fixed mesh.
More excellent ground, said transparent curtain wall is processed by poly (methyl methacrylate) plate, and said poly (methyl methacrylate) plate is embedded among the draw-in groove on the algae liquid spray unit supports frame.
More excellent ground, said spray thrower is the rectangular box of a hollow, and the bottom surface of the rectangular box of said hollow is opened some equally distributed apertures, and upper surface is installed the outer circulating tube interface.
More excellent ground, said spray thrower is that an xsect is semicircular long tube, the sealing two ends of said long tube, bottom surface is opened some equally distributed apertures, and last cambered surface is installed the outer circulating tube interface.
More excellent ground, said spray thrower is made up of some parallel and pipes that be interconnected, opens some equally distributed apertures on the pipe face of pipe, left and right sides installation outer circulating tube interface.
More excellent ground, said spray thrower is the rectangular box of a hollow, the rectangular box of said hollow leading flank be lower than trailing flank, upper surface is installed the outer circulating tube interface.
Compared with prior art, the utility model proposes a kind of plan of novel spray type bioreactor, in order to the efficient absorption of carbonic acid gas in the high-density culture that realizes little algae and the industrial gaseous waste.This bioreactor includes but are not limited to following advantage after further optimizing: (1) algae liquid spray has increased the transmitance of light, has improved the photosynthetic efficiency of frustule; (2) algae liquid spray has increased the contact area of algae liquid and gas, and spray and under algae liquid and the gas formation convection current of rising, improved the utilization ratio of frustule to carbonic acid gas; (3) algae liquid spray is less to the pressure that sidewall of reactor produces, and has reduced the difficulty that reactor drum makes up; (4) algae liquid spray can drive the effect that air flowing plays the cooling of algae liquid, and algae liquid can be brought in the reactor drum by the freezing air that reactor drum is outer in low level liquid storage tank process of flowing simultaneously, plays the effect of dual cooling; (5) utilize the gas lift mode to realize the Rapid Cycle of algae liquid, little to the frustule damage, can be used for the cultivation of little algae of acellular wall.
Description of drawings
Fig. 1 is the structural representation of the utility model spray-type bioreactor embodiment one;
Fig. 2 is the structural representation of the utility model spray-type bioreactor embodiment two;
Fig. 3 is a recycle pump recycle system fundamental diagram;
Fig. 4 is an air lift type recycle system fundamental diagram;
Fig. 5 A is algae liquid spray thrower type one structural representation;
Fig. 5 B is algae liquid spray thrower type two structural representations;
Fig. 5 C is algae liquid spray thrower type three structural representations;
Fig. 5 D is algae liquid spray thrower type four structural representations.
Embodiment
In theory, the bioreactor of efficiently removing carbonic acid gas need satisfy following two key factors: (1) little algae has high photosynthetic efficiency; (2) higher gas-liquid transfer efficiency.The utility model proposes a kind of novel spray type bioreactor on above-mentioned two key issue bases, efficient stabilizing carbon dioxide, and it is with low cost, amplifies easily, satisfies the needs of large scale culturing fully.Utilize this bioreactor to cultivate the little algae of the produce oil energy, method preferably is provided for solving environment and the dual crisis of the energy.
Particularly; The preferred embodiment of the utility model provides a kind of spray-type bioreactor; Be that the spray-type culturing system of light bioreactor comprises flat bioreactor, metal supporting frames, algae liquid spray unit, algae fluid circulation, industrial gaseous waste pretreatment unit, below respectively structure, function and the principle of each several part described.
Said flat bioreactor (hereinafter to be referred as dull and stereotyped reactor drum) is the transparent plate by some specific standards; Through the bonding transparent reaction container that forms of tackiness agent; Be positioned at the bottom of spray-type bioreactor (algae liquid spray unit), be mainly used in the temporary transient storage of cultivating algae liquid; Frustule in the dull and stereotyped reactor drum also can carry out photosynthesis simultaneously, realizes the accumulation of the preliminary fixing and living weight of carbonic acid gas.This flat bioreactor side is equipped with vent line interface, algae liquid outer circulating tube interface and prolong interface etc.Series connection amplifying technique about flat bioreactor details in another patented claim, in view of it is not the utility model key point, repeats no more at this.
Said metal supporting frames is installed in the upper surface of flat bioreactor, is mainly used in algae liquid and sprays unitary support and fixing.Leave the space between metal supporting frames and the flat bioreactor upper surface, guarantee that the dull and stereotyped bioreactor and the external world can carry out gaseous interchange.
Said algae liquid spray unit is the core texture of whole culture systems, comprises spray thrower and transparent curtain wall.Wherein the effect of spray thrower is that algae liquid is divided into some thinner liquid bundles, and the liquid bundle of generation is back in the process of dull and stereotyped bioreactor, can form convection current with the gas that rises, and helps the absorption of carbonic acid gas.Flow is become some thin liquid bundles, increased the contact area of frustule and gas, improved the solid carbon speed of little algae.Thin liquid Shu Buhui produces hydraulic pressure to the reactor drum side, can reduce the structure difficulty and the cost of reactor drum.Thin liquid bundle helps the transmission of light, can improve optical energy utilization efficiency.The air flowing that can drive algae liquid spray plays the effect of algae liquid cooling, and algae liquid can be brought in the reactor drum by the freezing air that reactor drum is outer in low level liquid storage tank process of flowing simultaneously, plays the effect of dual cooling.Transparent curtain wall is processed by transparence higher hard or soft material, and under the prerequisite that guarantees the light high transmission rate, it mainly acts on is to prevent the splash of algae liquid and stop algae liquid to contact with external environment.
The main effect of algae fluid circulation is the circulation that realizes algae liquid, guarantees that algae liquid can be got in the spray thrower by dull and stereotyped bioreactor fast.Algae strain for mechanical resistance is stronger can be adopted circulating pump system, can adopt the air lift type recycle system for the more weak algae strain of mechanical resistance (strain of acellular wall algae).
The industrial gaseous waste pretreatment unit mainly is responsible for removing in the industrial gaseous waste the deleterious SO of micro algae growth
x, NO
xDeng pollutent.
In order to make those skilled in the art understand the technical scheme of the utility model better, the utility model is done further to specify below in conjunction with accompanying drawing and specific embodiment.
Referring to Fig. 1 and Fig. 2, be two kinds of preferred embodiments of the utility model, wherein 1 is dull and stereotyped bioreactor; 11 is the prolong interface, and 12 is the outer circulating tube interface, and 13 is the vent line interface; 2 is metal supporting frames, and 21 is the reactor drum cover plate, and 31 is algae liquid spray thrower; 32 is transparent curtain wall, and 33 is the outer circulating tube interface.The function of each structure details in the utility model principle, no longer repeats at this.The mode of lacing wire or the external reinforcing scale of carrying out was amplified in dull and stereotyped bioreactor 1 can adopt, and its volume of culture is provided with by actual needs.Transparent curtain wall 32 can be processed by transparent plastic film or the thin poly (methyl methacrylate) plate of hard, and when selecting transparent plastic film (Fig. 1), available metal silk or plastic ties are made grid, transparent plastic film are fixed on it getting final product.When selecting hard to approach poly (methyl methacrylate) plate (Fig. 2), can the metal draw-in groove be installed on metal supporting frames 2, poly (methyl methacrylate) plate can embed wherein, can play the fixed effect equally.Water cooling unit that cooling circulating water is required or Air cooler need be purchased separately.Through the waste gas of industrial gaseous waste pretreatment unit rough handling, get in the dull and stereotyped bioreactor by vent line interface 13, carry out efficiently fixing.
Referring to Fig. 3 and Fig. 4, be two kinds of algae liquid circulation synoptic diagram of this culture systems.Fig. 3 is the fundamental diagram of circulating pump system, and its algae liquid round-robin propulsion source is a recycle pump, and algae liquid spray behind thorough mixing, under the pressurization of recycle pump, gets into spray thrower by outer circulating tube to dull and stereotyped bioreactor, accomplish the circulation of algae liquid.This recycle system can be used for the cultivation (chlorella etc.) of the stronger little algae of mechanical resistance.Fig. 4 is the air lift type recycle system, and this system is made up of structures such as header tank, outer circulating tube, sources of the gas.Source of the gas provides algae liquid round-robin power; After source of the gas blasted pressurized air, bubble moved upward under the effect of gas lift power, and the algae liquid that drives in the dull and stereotyped bioreactor gets in the header tank through outer circulating tube; Then entering spray thrower under the effect of gravity is accomplished the circulation of algae liquid.This Recycle design is less to the damage of frustule, the cultivation of the suitable little algae of acellular wall.
On the basis of following the utility model principle of design, can make up multiple multi-form spray thrower, illustrate as follows at present:
(1) the spray thrower type one
Referring to Fig. 5 A, by the rectangular box of hollow that plastics or metallic substance are processed, its bottom surface is opened some equally distributed small sircle holes, and upper surface is installed two groups of outer circulating tube interfaces, is used for the entering of algae liquid.
(2) the spray thrower type two
Referring to Fig. 5 B, the xsect of being processed by plastics or metallic substance is semicircular long tube, its sealing two ends, and bottom surface is opened some equally distributed small sircle holes, and the last cambered surface of semi-circular pipe is installed two groups of outer circulating tube interfaces, is used for the entering of algae liquid.
(3) the spray thrower type three
Referring to Fig. 5 C, by some parallel and be interconnected plastics tubing or stainless steel tube form, open some equally distributed small sircle holes on the pipe face, the outer circulating tube interface is installed in the left and right sides.
(4) the spray thrower type four
Referring to Fig. 5 D, profile is similar to spray thrower type one, and difference is that the lower surface of spray thrower type four is not opened small sircle hole, and the leading flank of spray thrower is lower than trailing flank, makes algae liquid to be flowed down by the front surface shown in Fig. 5 D, forms waterfall type algae flow.
As aforementioned, traditional bioreactor is used for removing of industrial gaseous waste carbonic acid gas, and its efficient is lower, and the output of little algal biomass is not high, and the reactor drum construction cost is expensive, and scale is amplified difficulty, and the luminous energy transfer efficiency is low.
And the utility model proposes a kind of novel spray type photo-bioreactor system, first algae liquid spraying technique is introduced in the design of bioreactor, has improved the production efficiency of bioreactor greatly.In practical study with in producing, solved following key technical problem: the low cost of (1) bioreactor makes up and scale is amplified; (2) carbonic acid gas is efficient fixing; (3) the luminous energy transfer efficiency is high; (4) gas-liquid mass transfer efficient is high; (5) temperature with high efficiency of nutrient solution.
It below only is the preferred implementation of the utility model; Its key point is through the mode that sprays algae liquid to be divided into some thinner liquid bundles; Increase the transmitance and the gas-liquid rate of mass transfer of light, improved the carbon dioxide fixation efficient of little algae, realized the fast cooling of algae liquid.Should be pointed out that above-mentioned preferred implementation should not be regarded as the restriction to the utility model, the protection domain of the utility model should be as the criterion with claim institute restricted portion.For those skilled in the art, in spirit that does not break away from the utility model and scope, can also make some improvement and retouching, these improvement and retouching also should be regarded as the protection domain of the utility model.
Claims (10)
1. spray-type bioreactor; It is characterized in that; Comprise flat bioreactor, be arranged at the algae liquid spray unit of said flat bioreactor top, the industrial gaseous waste pretreatment unit that inserts said flat bioreactor and driving algae liquid round-robin algae fluid circulation between said flat bioreactor and said algae liquid spray unit; Wherein said algae liquid spray unit comprises: spray thrower, in order to algae liquid under the dispersion train; Transparent curtain wall is in order to prevent the splash of algae liquid and to stop algae liquid to contact with external environment.
2. spray-type bioreactor as claimed in claim 1; It is characterized in that; The transparent reaction container of said flat bioreactor for being bonded by some predetermined dimension transparent plates, the side of said transparent reaction container is equipped with ventpipe interface, outer circulating tube interface and prolong interface.
3. spray-type bioreactor as claimed in claim 1 is characterized in that, said algae fluid circulation comprises: outer circulating tube is communicated with said flat bioreactor and said algae liquid spray unit; Recycle pump is positioned on the said outer circulating tube.
4. spray-type bioreactor as claimed in claim 1 is characterized in that, said algae fluid circulation comprises: header tank, its fluid inlet and liquid outlet are communicated with said flat bioreactor and said algae liquid spray unit through outer circulating tube respectively; Source of the gas, its air feed port is connected on the riser culverts of said outer circulating tube.
5. spray-type bioreactor as claimed in claim 1 is characterized in that, said transparent curtain wall is processed by transparent plastic film, and said transparent plastic film is covered on the fixed mesh.
6. spray-type bioreactor as claimed in claim 1 is characterized in that, said transparent curtain wall is processed by poly (methyl methacrylate) plate, and said poly (methyl methacrylate) plate is embedded among the draw-in groove on the algae liquid spray unit supports frame.
7. spray-type bioreactor as claimed in claim 1 is characterized in that, said spray thrower is the rectangular box of a hollow, and the bottom surface of the rectangular box of said hollow is opened some equally distributed apertures, and upper surface is installed the outer circulating tube interface.
8. spray-type bioreactor as claimed in claim 1 is characterized in that, said spray thrower is that an xsect is semicircular long tube, the sealing two ends of said long tube, and bottom surface is opened some equally distributed apertures, and last cambered surface is installed the outer circulating tube interface.
9. spray-type bioreactor as claimed in claim 1 is characterized in that, said spray thrower is made up of some parallel and pipes that be interconnected, opens some equally distributed apertures on the pipe face of pipe, and the outer circulating tube interface is installed in the left and right sides.
10. spray-type bioreactor as claimed in claim 1 is characterized in that, said spray thrower is the rectangular box of a hollow, the rectangular box of said hollow leading flank be lower than trailing flank, upper surface is installed the outer circulating tube interface.
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|---|---|---|---|
| CN 201120319664 CN202297574U (en) | 2011-08-29 | 2011-08-29 | Shower type photo-bioreactor |
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|---|---|---|---|
| CN 201120319664 CN202297574U (en) | 2011-08-29 | 2011-08-29 | Shower type photo-bioreactor |
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Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105985910A (en) * | 2015-03-05 | 2016-10-05 | 华东理工大学 | Novel method and process for carbon supplement during microalgae culture |
| CN108102876A (en) * | 2017-11-10 | 2018-06-01 | 蒋花 | A kind of continuous harvesting device of microalgae and method |
-
2011
- 2011-08-29 CN CN 201120319664 patent/CN202297574U/en not_active Expired - Fee Related
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105985910A (en) * | 2015-03-05 | 2016-10-05 | 华东理工大学 | Novel method and process for carbon supplement during microalgae culture |
| CN108102876A (en) * | 2017-11-10 | 2018-06-01 | 蒋花 | A kind of continuous harvesting device of microalgae and method |
| CN108102876B (en) * | 2017-11-10 | 2021-10-12 | 日照市海洋与渔业研究所 | Continuous microalgae harvesting device and method |
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