CN105087374A - Carbon source supply system for spirulina cultivated in pool - Google Patents
Carbon source supply system for spirulina cultivated in pool Download PDFInfo
- Publication number
- CN105087374A CN105087374A CN201510513015.2A CN201510513015A CN105087374A CN 105087374 A CN105087374 A CN 105087374A CN 201510513015 A CN201510513015 A CN 201510513015A CN 105087374 A CN105087374 A CN 105087374A
- Authority
- CN
- China
- Prior art keywords
- cultivation pool
- spirulina
- carbon source
- ejector
- 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.)
- Pending
Links
Classifications
-
- 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
- C12M43/00—Combinations of bioreactors or fermenters with other apparatus
- C12M43/08—Bioreactors or fermenters combined with devices or plants for production of electricity
-
- 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
- C12M23/22—Transparent or translucent parts
-
- 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
- C12M41/00—Means for regulation, monitoring, measurement or control, e.g. flow regulation
- C12M41/12—Means for regulation, monitoring, measurement or control, e.g. flow regulation of temperature
-
- 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
- C12M41/00—Means for regulation, monitoring, measurement or control, e.g. flow regulation
- C12M41/12—Means for regulation, monitoring, measurement or control, e.g. flow regulation of temperature
- C12M41/18—Heat exchange systems, e.g. heat jackets or outer envelopes
-
- 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
- C12M43/00—Combinations of bioreactors or fermenters with other apparatus
- C12M43/06—Photobioreactors combined with devices or plants for gas production different from a bioreactor of fermenter
Abstract
The invention discloses a carbon source supply system for spirulina cultivated in a pool. The carbon source supply system for spirulina cultivated in the pool comprises a dry ice storage tank, a vaporizer, a heat exchanger, a jet device and a microalgae cultivation system, wherein the dry ice storage tank, the vaporizer and the heat exchanger are connected through a pipeline in turn; the jet device is provided with a first inlet, a second inlet and an outlet; the first inlet is connected with the heat exchanger through a pipeline; the second inlet is connected with a culture solution tube; and the outlet is connected with the microalgae cultivation system through a pipeline. The carbon source supply system disclosed by the invention is reliable in structure, energy-saving and environmentally friendly, simple and feasible, and the growth period of spirulina is shortened by 1.5 times.
Description
Technical field
The present invention relates to algal culture technical field, particularly spirulina carbon source plenum system is supported in a kind of pond.
Background technology
Spirulina contains multiple beneficial growth in humans and healthy aquatic bacterium algae, and it eats and pharmaceutical use is more and more subject to social favor.Thus, in recent years spirulina propagate industry fast development artificially.In breeding process, the pH of growth of spirulina platensis is 8-11.
Carbonic acid gas is the important substance of algal grown, and after algae absorbs, carbonic acid gas carries out photosynthesis in suitable temperature light situation, completes the growth of algae.Domestic and international in Outdoor large-scale cultivation spirulina at present, the water-soluble mode discharging carbon dioxide of general employing sodium bicarbonate, supplements the carbon source fertilizer that growth of spirulina platensis is necessary.Now the utilization ratio of carbonic acid gas is low, is generally 65%, causes the waste of resource.Carbonic acid gas is not easily closed and causes leakage, enters in air, produces Greenhouse effect.Therefore cause algal grown speed slow, aquaculture cost is high.
At present, lack a kind of pond can shortening the culture-cycle of spirulina and support spirulina carbon source plenum system.
Summary of the invention
The object of this invention is to provide a kind of pond can shortening the culture-cycle of spirulina and support spirulina carbon source plenum system.
In order to realize above-mentioned technical problem, technical scheme provided by the invention is: the invention provides a kind of pond and support spirulina carbon source plenum system, described pond is supported spirulina carbon source plenum system and is comprised dry ice hold-up vessel, vaporizer, interchanger, ejector and both culturing microalgae system, and described dry ice hold-up vessel, vaporizer, interchanger are connected successively by pipeline; Described ejector is provided with the first entrance, the second entrance and exit, and described first entrance is connected by pipeline with interchanger; Described second entrance is connected with nutrient solution pipe, and described outlet is connected by pipeline with both culturing microalgae system;
Described vaporizer comprises housing, is provided with induction trunk in described housing, is provided with throttling element and described throttling element upper end is provided with flow blocking element in described induction trunk; With at least one fuel inlet, described fuel inlet at the communicating downstream of described flow blocking element in described induction trunk; And flowrate control valve, described flowrate control valve controls the fuel being transported to described fuel inlet, is provided with at least one import that refuels, described in the import that refuels be communicated in described induction trunk in the upper end of described flow blocking element;
Described both culturing microalgae system comprises greenhouse, pump, cultivation pool and inflation mechanism;
The top in described greenhouse is provided with spaced solar panel, described inflation mechanism be arranged on cultivation pool bottom outside and with cultivation pool bottom outer wall Joint;
Described cultivation pool is arranged on the inside in greenhouse, described cultivation pool is provided with the first fluid inlet and the second liquid outlet, described transparent tube is provided with the second fluid inlet and the second liquid outlet, is provided with light aid in described cultivation pool; Described first fluid inlet and the first liquid outlet are arranged in the bottom outer wall of cultivation pool;
Be provided with the nutrient solution cultivating energy algae in described cultivation pool, the second fluid inlet of described transparent tube is connected with the first liquid outlet of cultivation pool by pump; Second liquid outlet of described transparent tube is connected with the first fluid inlet of cultivation pool;
Described light aid be arranged on cultivation pool bottom and with the inwall Joint of cultivation pool.
Described inflation mechanism is made up of air pump, tracheae and ventilative ring, and described air pump, tracheae are connected with ventilative ring.
Further, described ejector is Venturi ejector.
Further, the connecting tube of described ejector and described both culturing microalgae system is provided with liquid meter.
Further, described interchanger is round shape.
Further, described dry ice hold-up vessel, vaporizer, interchanger, ejector and the both culturing microalgae system integration are arranged in casing, and described casing quantity is one or more, is connected in series mutually by pipeline.
Beneficial effect: present system is rational in infrastructure, energy-conserving and environment-protective, simple and easy to do, the growth cycle 1.5 times of spirulina can be shortened.Relative to prior art, tool of the present invention has the following advantages:
(1) carbon dioxide is discharged by dry ice, the content that the absorption that effectively can increase carbon dioxide in culturing liquid is dissolved and speed, greatly can improve the utilization ratio of carbonic acid gas, eliminate carbon dioxide and the pollution to atmospheric environment thereof, reduce the aquaculture cost of spirulina, shorten the culture-cycle of spirulina.
(2) invention increases the utilization ratio of carbonic acid gas, facilitate the quick growth of algae, the aquaculture cost of spirulina is declined to a great extent, reduces more than 20%.Do not use sodium bicarbonate, carbonic acid gas can extract from industrial gaseous waste, and cost is low, reduces the discharge of carbon dioxide; Can also releasing oxygen after algae absorbing carbon dioxide, can purify air.Ensure that the fine quality of product, all low international standards of indices such as the heavy metal of product and microorganism.
(3) the present invention is provided with solar panel on top, greenhouse, it is the effect in order to play shading storage power when illumination is too strong, because illumination is too strong to the unfavorable suppression algal grown of algal grown, when illumination deficiency time, the energy that at this time solar panel stores can provide the energy for light-supplementing system.In intensity of illumination lower than 300 μm of ol/m
2during/s, the biomass of spirulina presents ascendant trend along with the enhancing of intensity of illumination, when intensity of illumination is 450 μm of ol/m
2during/s, frustule mortality, presents white.The too high meeting of light intensity significantly suppresses biological growth and CO
2fixed rate.At 75 μm of ol/m
2under the intensity of illumination of/s, there is an obvious lag phase in early growth period.With 75 μm of ol/m
2/ s compares, 150 μm of ol/m
2/ s and 300 μm ol/m
2under/s intensity of illumination, frustule growth is in earlier stage closely similar, and stage finds 300 μm of ol/m
2the illumination of/s is more favourable to frustule growth, and along with the accumulation of cellular biomass, this advantage is more remarkable.
(4) the general illumination of the great Chi under solar panel is at 4-6Wlux, outdoor illumination is 10W, every day, growth velocity was about 0.1, adopting pipeline to cultivate speed is about its 2-3 times, if adopt the solar panel 4 of 2/3rds, the growth of great Chi by reduction by 2/3rds, and supplements cultivation with pipeline, and growth velocity will be much higher than original closed cultivation.
(5) during overcast and rainy and night, illumination is not enough, and the colored led lamp in glass sunlight house can be utilized to supplement light source, allows algae can 24 hours growth, improves the yield and quality of algae.When illumination deficiency, nutrient solution 10 is looped around the top in greenhouse 1 by transparent tube 9, and finally enters cultivation pool 2, and it is more that the algae in such transparent tube 9 can obtain illumination, makes growth better, the cycle time of algae culture.
(6) the combination cultivation of the solid of plane can make full use of limited soil.Utilization rate of carbon dioxide can be improved fully, also can solve the emission problem of some enterprise's carbonic acid gas, the covert production capacity improving these enterprises.
Accompanying drawing explanation
Fig. 1 is schematic diagram of the present invention;
Wherein: 1 dry ice hold-up vessel; 2 interchanger; 3 vaporizers; 4 ejectors; 5 both culturing microalgae systems; 6 first entrances; 7 second entrances; 8 outlets.
Embodiment
In order to illustrate technical scheme of the present invention and technical purpose, below in conjunction with figure and embodiment, the present invention is described further.
Embodiment 1
As shown in Figure 1, the invention provides a kind of pond and support spirulina carbon source plenum system, described pond is supported spirulina carbon source plenum system and is comprised dry ice hold-up vessel 1, vaporizer 2, interchanger 3, ejector 4 and both culturing microalgae system 5, and described dry ice hold-up vessel 1, vaporizer 2, interchanger 3 are connected successively by pipeline; Described ejector is provided with the first entrance 6, second entrance 7 and outlet 8, and described first entrance 6 is connected by pipeline with interchanger 3; Described second entrance 7 is connected with nutrient solution pipe, and described outlet 8 is connected by pipeline with both culturing microalgae system 5.
Described vaporizer 2 comprises housing, fuel inlet, flowrate control valve and the import that refuels, and is provided with induction trunk in described housing, is provided with throttling element and described throttling element upper end is provided with flow blocking element in described induction trunk; Described fuel inlet at the communicating downstream of described flow blocking element in described induction trunk; Described flowrate control valve controls the fuel being transported to described fuel inlet, described in the import that refuels be communicated in described induction trunk in the upper end of described flow blocking element.
Described both culturing microalgae system 5 comprises greenhouse, pump, cultivation pool and inflation mechanism;
The top in described greenhouse is provided with spaced solar panel, described inflation mechanism be arranged on cultivation pool bottom outside and with cultivation pool bottom outer wall Joint;
Described cultivation pool is arranged on the inside in greenhouse, described cultivation pool is provided with the first fluid inlet and the second liquid outlet, described transparent tube is provided with the second fluid inlet and the second liquid outlet, is provided with light aid in described cultivation pool; Described first fluid inlet and the first liquid outlet are arranged in the bottom outer wall of cultivation pool;
Be provided with the nutrient solution cultivating energy algae in described cultivation pool, the second fluid inlet of described transparent tube is connected with the first liquid outlet of cultivation pool by pump; Second liquid outlet of described transparent tube is connected with the first fluid inlet of cultivation pool;
Described light aid be arranged on cultivation pool bottom and with the inwall Joint of cultivation pool.
Described inflation mechanism is made up of air pump, tracheae and ventilative ring, and described air pump, tracheae are connected with ventilative ring.
Described ejector 4 is Venturi ejector.
Described ejector 4 and the connecting tube of described both culturing microalgae system 5 are provided with liquid meter.
Described interchanger 2 is round shape.
Described dry ice hold-up vessel 1, interchanger 2, vaporizer 3, ejector 4 and both culturing microalgae system 5 integrated installation are in casing, and described casing quantity is one or more, is connected in series mutually by pipeline.
Present system is rational in infrastructure, energy-conserving and environment-protective, simple and easy to do, can shorten the growth cycle 1.5 times of spirulina.Relative to prior art, tool of the present invention has the following advantages:
(1) carbon dioxide is discharged by dry ice, the content that the absorption that effectively can increase carbon dioxide in culturing liquid is dissolved and speed, greatly can improve the utilization ratio of carbonic acid gas, eliminate carbon dioxide and the pollution to atmospheric environment thereof, reduce the aquaculture cost of spirulina, shorten the culture-cycle of spirulina.
(2) invention increases the utilization ratio of carbonic acid gas, facilitate the quick growth of algae, the aquaculture cost of spirulina is declined to a great extent, reduces more than 20%.Do not use sodium bicarbonate, carbonic acid gas can extract from industrial gaseous waste, and cost is low, reduces the discharge of carbon dioxide; Can also releasing oxygen after algae absorbing carbon dioxide, can purify air.Ensure that the fine quality of product, all low international standards of indices such as the heavy metal of product and microorganism.
(3) the present invention is provided with solar panel on top, greenhouse, it is the effect in order to play shading storage power when illumination is too strong, because illumination is too strong to the unfavorable suppression algal grown of algal grown, when illumination deficiency time, the energy that at this time solar panel stores can provide the energy for light-supplementing system.In intensity of illumination lower than 300 μm of ol/m
2during/s, the biomass of spirulina presents ascendant trend along with the enhancing of intensity of illumination, when intensity of illumination is 450 μm of ol/m
2during/s, frustule mortality, presents white.The too high meeting of light intensity significantly suppresses biological growth and CO
2fixed rate.At 75 μm of ol/m
2under the intensity of illumination of/s, there is an obvious lag phase in early growth period.With 75 μm of ol/m
2/ s compares, 150 μm of ol/m
2/ s and 300 μm ol/m
2under/s intensity of illumination, frustule growth is in earlier stage closely similar, and stage finds 300 μm of ol/m
2the illumination of/s is more favourable to frustule growth, and along with the accumulation of cellular biomass, this advantage is more remarkable.
(4) the general illumination of the great Chi under solar panel is at 4-6Wlux, outdoor illumination is 10W, every day, growth velocity was about 0.1, adopting pipeline to cultivate speed is about its 2-3 times, if adopt the solar panel 4 of 2/3rds, the growth of great Chi by reduction by 2/3rds, and supplements cultivation with pipeline, and growth velocity will be much higher than original closed cultivation.
(5) during overcast and rainy and night, illumination is not enough, and the colored led lamp in glass sunlight house can be utilized to supplement light source, allows algae can 24 hours growth, improves the yield and quality of algae.When illumination deficiency, nutrient solution 10 is looped around the top in greenhouse 1 by transparent tube 9, and finally enters cultivation pool 2, and it is more that the algae in such transparent tube 9 can obtain illumination, makes growth better, the cycle time of algae culture.
(6) the combination cultivation of the solid of plane can make full use of limited soil.Utilization rate of carbon dioxide can be improved fully, also can solve the emission problem of some enterprise's carbonic acid gas, the covert production capacity improving these enterprises.
Although more employ the terms such as dry ice hold-up vessel 1, interchanger 2, vaporizer 3, ejector 4, cultivation pool 5, first entrance 6, second entrance 7, outlet 8 herein, do not get rid of the possibility using other term.These terms are used to be only used to describe and explain essence of the present invention more easily; The restriction that they are construed to any one additional is all contrary with spirit of the present invention.
More than show and describe ultimate principle of the present invention, principal character and advantage of the present invention.The technician of the industry should understand; the present invention is not restricted to the described embodiments; what describe in above-described embodiment and specification sheets just illustrates principle of the present invention; without departing from the spirit and scope of the present invention; the present invention also has various changes and modifications, and application claims protection domain is defined by appending claims, specification sheets and equivalent thereof.
Claims (5)
1. spirulina carbon source plenum system is supported in a pond, it is characterized in that: described pond is supported spirulina carbon source plenum system and comprised dry ice hold-up vessel, vaporizer, interchanger, ejector and both culturing microalgae system, and described dry ice hold-up vessel, vaporizer, interchanger are connected successively by pipeline; Described ejector is provided with the first entrance, the second entrance and exit, and described first entrance is connected by pipeline with interchanger; Described second entrance is connected with nutrient solution pipe, and described outlet is connected by pipeline with both culturing microalgae system;
Described vaporizer comprises housing, is provided with induction trunk in described housing, is provided with throttling element and described throttling element upper end is provided with flow blocking element in described induction trunk; With at least one fuel inlet, described fuel inlet at the communicating downstream of described flow blocking element in described induction trunk; And flowrate control valve, described flowrate control valve controls the fuel being transported to described fuel inlet, is provided with at least one import that refuels, described in the import that refuels be communicated in described induction trunk in the upper end of described flow blocking element;
Described both culturing microalgae system comprises greenhouse, pump, cultivation pool and inflation mechanism;
The top in described greenhouse is provided with spaced solar panel, described inflation mechanism be arranged on cultivation pool bottom outside and with cultivation pool bottom outer wall Joint;
Described cultivation pool is arranged on the inside in greenhouse, described cultivation pool is provided with the first fluid inlet and the second liquid outlet, described transparent tube is provided with the second fluid inlet and the second liquid outlet, is provided with light aid in described cultivation pool; Described first fluid inlet and the first liquid outlet are arranged in the bottom outer wall of cultivation pool;
Be provided with the nutrient solution cultivating energy algae in described cultivation pool, the second fluid inlet of described transparent tube is connected with the first liquid outlet of cultivation pool by pump; Second liquid outlet of described transparent tube is connected with the first fluid inlet of cultivation pool;
Described light aid be arranged on cultivation pool bottom and with the inwall Joint of cultivation pool.
Described inflation mechanism is made up of air pump, tracheae and ventilative ring, and described air pump, tracheae are connected with ventilative ring.
2. spirulina carbon source plenum system is supported in pond according to claim 1, it is characterized in that: described ejector is Venturi ejector.
3. spirulina carbon source plenum system is supported in pond according to claim 1, it is characterized in that: the connecting tube of described ejector and described both culturing microalgae system is provided with liquid meter.
4. spirulina carbon source plenum system is supported in pond according to claim 1, it is characterized in that: described interchanger is round shape.
5. spirulina carbon source plenum system is supported in the pond according to any one of Claims 1-4, it is characterized in that: described dry ice hold-up vessel, vaporizer, interchanger, ejector and the both culturing microalgae system integration are arranged in casing, described casing quantity is one or more, is connected in series mutually by pipeline.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201510513015.2A CN105087374A (en) | 2015-08-19 | 2015-08-19 | Carbon source supply system for spirulina cultivated in pool |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201510513015.2A CN105087374A (en) | 2015-08-19 | 2015-08-19 | Carbon source supply system for spirulina cultivated in pool |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN105087374A true CN105087374A (en) | 2015-11-25 |
Family
ID=54568712
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201510513015.2A Pending CN105087374A (en) | 2015-08-19 | 2015-08-19 | Carbon source supply system for spirulina cultivated in pool |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN105087374A (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107118953A (en) * | 2017-04-26 | 2017-09-01 | 重庆大学 | Using biomass slurry as the solar heat chemical conversion system and method for collection hot working fluid |
| CN110643514A (en) * | 2019-10-14 | 2020-01-03 | 贵州民族大学 | Method for culturing porphyridium by using culture wastewater |
| CN115044475A (en) * | 2022-07-29 | 2022-09-13 | 东方新大泽天然生物科技有限公司 | Method for culturing microalgae by combining photovoltaic panel |
Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN201180138Y (en) * | 2008-03-12 | 2009-01-14 | 崔致宪 | Energy conservation environment friendly semiclosed algae bioreactor |
| CN101597567A (en) * | 2008-06-05 | 2009-12-09 | 新奥科技发展有限公司 | Bioreactor |
| CN102022227A (en) * | 2009-09-22 | 2011-04-20 | 安德烈亚斯.斯蒂尔两合公司 | Carburetor |
| CN202193783U (en) * | 2011-08-26 | 2012-04-18 | 新奥科技发展有限公司 | Microorganism cultivation system |
| CN202322848U (en) * | 2011-11-16 | 2012-07-11 | 新奥科技发展有限公司 | Photosynthetic microorganism culture equipment |
-
2015
- 2015-08-19 CN CN201510513015.2A patent/CN105087374A/en active Pending
Patent Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN201180138Y (en) * | 2008-03-12 | 2009-01-14 | 崔致宪 | Energy conservation environment friendly semiclosed algae bioreactor |
| CN101597567A (en) * | 2008-06-05 | 2009-12-09 | 新奥科技发展有限公司 | Bioreactor |
| CN102022227A (en) * | 2009-09-22 | 2011-04-20 | 安德烈亚斯.斯蒂尔两合公司 | Carburetor |
| CN202193783U (en) * | 2011-08-26 | 2012-04-18 | 新奥科技发展有限公司 | Microorganism cultivation system |
| CN202322848U (en) * | 2011-11-16 | 2012-07-11 | 新奥科技发展有限公司 | Photosynthetic microorganism culture equipment |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107118953A (en) * | 2017-04-26 | 2017-09-01 | 重庆大学 | Using biomass slurry as the solar heat chemical conversion system and method for collection hot working fluid |
| CN110643514A (en) * | 2019-10-14 | 2020-01-03 | 贵州民族大学 | Method for culturing porphyridium by using culture wastewater |
| CN115044475A (en) * | 2022-07-29 | 2022-09-13 | 东方新大泽天然生物科技有限公司 | Method for culturing microalgae by combining photovoltaic panel |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN102134553B (en) | Tubular photobioreactor and system and method for culturing microalgae cells | |
| CN101575567A (en) | Method for culturing microalgae by illumination way and reactor thereof | |
| CN105039138A (en) | Microalgae culture system with solar cell panels and culture method thereof | |
| CN101513174A (en) | Circulating water culture system with low energy consumption | |
| CN107189930A (en) | Indoor microalgae culture system and its cultural method | |
| CN1475558A (en) | Photosynthesis bioreactor system for industrial production of micro algae | |
| CN105087374A (en) | Carbon source supply system for spirulina cultivated in pool | |
| CN106957790B (en) | A kind of semi-enclosed culture pipeline of microalgae algae optical-biological reaction and its application method | |
| CN103602579B (en) | Pipeline-type photobioreactor for scale culture of microalgae | |
| CN101906380B (en) | Seal type pipeline culture device of bait microalgae and microalgae pipeline culture method | |
| CN204474658U (en) | Multistage potential energy differential driving microdisk electrode dedicated optical bioreactor system | |
| CN201729830U (en) | Sealed pipeline culturing device for bait microalgae | |
| CN2688718Y (en) | Spiral pipe optical biological reactor | |
| CN102559478B (en) | Controllable slope type microalgae cultivation system and microalgae cultivation method thereof | |
| JP5324532B2 (en) | Circulating photobioreactor | |
| CN202881248U (en) | Simulation device for large-scale culture of microalgae | |
| CN106635768B (en) | Biological microalgae photosynthetic reactor and its application method | |
| CN205874418U (en) | Domestic spirulina culture apparatus | |
| CN202465662U (en) | Slope controllable microalgae breeding system | |
| CN205035361U (en) | Photobioreactor that little algae was cultivateed | |
| CN103131627A (en) | Light organism reaction device and application | |
| CN106010951A (en) | Household spirulina culture device | |
| CN209643526U (en) | Algal culture pond suitable for pearl culture | |
| CN202925000U (en) | Split type microalgae cultivation device | |
| CN206502810U (en) | Spirulina breeding system |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C06 | Publication | ||
| PB01 | Publication | ||
| C10 | Entry into substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| RJ01 | Rejection of invention patent application after publication | ||
| RJ01 | Rejection of invention patent application after publication |
Application publication date: 20151125 |