CN2885390Y - Carbon dioxide conversion device for biological photosynthesis reactor - Google Patents
Carbon dioxide conversion device for biological photosynthesis reactor Download PDFInfo
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- CN2885390Y CN2885390Y CNU2006200228659U CN200620022865U CN2885390Y CN 2885390 Y CN2885390 Y CN 2885390Y CN U2006200228659 U CNU2006200228659 U CN U2006200228659U CN 200620022865 U CN200620022865 U CN 200620022865U CN 2885390 Y CN2885390 Y CN 2885390Y
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- carbon dioxide
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- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 title claims abstract description 166
- 229910002092 carbon dioxide Inorganic materials 0.000 title claims abstract description 83
- 239000001569 carbon dioxide Substances 0.000 title claims abstract description 79
- 238000006243 chemical reaction Methods 0.000 title claims abstract description 59
- 230000029553 photosynthesis Effects 0.000 title abstract description 7
- 238000010672 photosynthesis Methods 0.000 title abstract description 7
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 claims abstract description 29
- 229910052760 oxygen Inorganic materials 0.000 claims abstract description 29
- 239000001301 oxygen Substances 0.000 claims abstract description 29
- 230000000243 photosynthetic effect Effects 0.000 claims abstract description 24
- 239000007789 gas Substances 0.000 claims abstract description 21
- 238000000926 separation method Methods 0.000 claims abstract description 6
- 238000003860 storage Methods 0.000 claims abstract description 5
- 239000007788 liquid Substances 0.000 claims description 39
- 239000000725 suspension Substances 0.000 claims description 16
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 13
- 244000005700 microbiome Species 0.000 claims description 12
- 238000011084 recovery Methods 0.000 claims description 12
- 238000002407 reforming Methods 0.000 claims description 12
- 238000005119 centrifugation Methods 0.000 claims description 9
- 230000000813 microbial effect Effects 0.000 claims description 9
- 235000005976 Citrus sinensis Nutrition 0.000 claims description 6
- 240000002319 Citrus sinensis Species 0.000 claims description 6
- 108091028732 Concatemer Proteins 0.000 claims description 6
- 230000000694 effects Effects 0.000 claims description 6
- 241000233855 Orchidaceae Species 0.000 claims description 5
- 238000001816 cooling Methods 0.000 claims description 4
- 238000009826 distribution Methods 0.000 claims description 3
- 229920002521 macromolecule Polymers 0.000 claims description 3
- 229910052761 rare earth metal Inorganic materials 0.000 claims description 3
- 150000002910 rare earth metals Chemical class 0.000 claims description 3
- 239000012780 transparent material Substances 0.000 claims description 3
- 238000001914 filtration Methods 0.000 abstract description 2
- 238000005507 spraying Methods 0.000 abstract 2
- 230000001131 transforming effect Effects 0.000 abstract 2
- 238000003915 air pollution Methods 0.000 abstract 1
- 238000010961 commercial manufacture process Methods 0.000 abstract 1
- 238000005516 engineering process Methods 0.000 description 12
- 238000004519 manufacturing process Methods 0.000 description 7
- 241000195493 Cryptophyta Species 0.000 description 5
- 238000000034 method Methods 0.000 description 4
- 241000196324 Embryophyta Species 0.000 description 3
- 238000006477 desulfuration reaction Methods 0.000 description 3
- 230000023556 desulfurization Effects 0.000 description 3
- 239000005431 greenhouse gas Substances 0.000 description 3
- 230000000087 stabilizing effect Effects 0.000 description 3
- 238000003756 stirring Methods 0.000 description 3
- 239000000126 substance Substances 0.000 description 3
- 239000002699 waste material Substances 0.000 description 3
- 229910000831 Steel Inorganic materials 0.000 description 2
- 239000003054 catalyst Substances 0.000 description 2
- 238000007599 discharging Methods 0.000 description 2
- 230000004992 fission Effects 0.000 description 2
- 239000000446 fuel Substances 0.000 description 2
- 239000000203 mixture Substances 0.000 description 2
- 239000010959 steel Substances 0.000 description 2
- 238000010792 warming Methods 0.000 description 2
- 238000006424 Flood reaction Methods 0.000 description 1
- 239000002253 acid Substances 0.000 description 1
- 230000005791 algae growth Effects 0.000 description 1
- 238000004577 artificial photosynthesis Methods 0.000 description 1
- 238000009903 catalytic hydrogenation reaction Methods 0.000 description 1
- 239000003245 coal Substances 0.000 description 1
- 238000002485 combustion reaction Methods 0.000 description 1
- 239000003814 drug Substances 0.000 description 1
- 238000003487 electrochemical reaction Methods 0.000 description 1
- 210000003608 fece Anatomy 0.000 description 1
- 239000003337 fertilizer Substances 0.000 description 1
- 235000013305 food Nutrition 0.000 description 1
- 239000003365 glass fiber Substances 0.000 description 1
- 230000012010 growth Effects 0.000 description 1
- 229910052500 inorganic mineral Inorganic materials 0.000 description 1
- 239000003077 lignite Substances 0.000 description 1
- 239000011707 mineral Substances 0.000 description 1
- 150000002894 organic compounds Chemical class 0.000 description 1
- 238000004064 recycling Methods 0.000 description 1
- 230000000630 rising effect Effects 0.000 description 1
- 239000002689 soil Substances 0.000 description 1
- 239000002912 waste gas Substances 0.000 description 1
- 239000002023 wood Substances 0.000 description 1
Images
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02A—TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
- Y02A50/00—TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE in human health protection, e.g. against extreme weather
- Y02A50/20—Air quality improvement or preservation, e.g. vehicle emission control or emission reduction by using catalytic converters
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- Apparatus Associated With Microorganisms And Enzymes (AREA)
Abstract
The utility model relates to a device capable of transforming carbon dioxide gas into oxygen by use of biological photosynthetic reactor. The carbon dioxide gas transforming device using biological photosynthetic reactor comprises a carbon dioxide filtering and desulfurating device communicated with the carbon dioxide discharge source, a carbon dioxide gas storage device, a carbon dioxide spraying and flow-disturbing system, a two-cycle biological reaction tower, a photosynthetic light source control system, a temperature-control circulating system, a oxygen collection tower, a microbe separation and collecting system and a plurality of tubes. The two-cycle biological reaction tower is composed of an inner jar and an outer jar. The carbon dioxide spraying and flow-disturbing system and the diode photosynthetic light source control system are provided inside the inner jar and the temperature-control circulating system is arranged at the bottom of the outer jar. The oxygen collection tower is connected with the bottom of the inner jar through line pipes, gas valves and gas centrifugal pumps. The lower part of the inner jar is provided and connected with microbe separation and collecting system through line pipes. The utility model is characterized in that the discarded carbon dioxide gas can be transformed into oxygen completely by use of biological photosynthesis and the commercial manufacture can be launched to consume carbon dioxide in large amounts, thereby effectively resolving the air pollution caused by carbon dioxide.
Description
Technical field
The utility model relates to a kind of biological photo-synthetic reactor carbon dioxide reforming unit, particularly relates to a kind of device that utilizes biological photo-synthetic reactor that carbon dioxide is used and change into oxygen.
Background technology
At present, greenhouse effects and global warming problem have become the focus of global environment problem.The variation of global climate has " artificial influence factor ", be exactly the greenhouse gases that cause such as modern industry double discharge, can make earth 1.1-3.3 degree centigrade of temperature rising in following 100 years, and be exactly main greenhouse gases from the carbon dioxide of burning mineral fuel.Be discharged into the carbon dioxide in the atmosphere, can the heat of the earth be covered as the greenhouse, make global warming, cause sea-level rise at last, the soil, strand floods, the change of earth whole ecological environment.Should how to utilize problem fully at the carbon dioxide in the production of energy, obtain countries in the world and generally paid attention to, propose various solutions at present.
The German Research personnel Mi Xiaaier Mel Buddhist nun of section installs the bioreactor of meter, with glass fiber cable sunlight is led the big case of steel (volume the is 6000 liters) lining that one of people is placed with algae exactly, makes to be full of daylight in the case.Make then the waste gas that contains carbon dioxide from adjacent brown coal power plant in desulfurization apparatus flows into case, the liquid dung in rural area is flowed in case by another root pipeline.So the algae in the case just begins " work ".They produce medicine and the operable high value organic compound of food industry by photosynthetic mode with disgusting batching.He has built a cover experimental facilities in it is located at the laboratory of University of Cologne, in this cover experimental facilities, the carbon dioxide that small aquatic organism discharges coal combustion almost all utilizes and becomes oxygen.With the method for Mel Ke Nian, can make the greenhouse gases composition in the smog of thermal power plant reduce to one thousandth.If the algae device is all installed in all factories and thermal power plant, about 1,000,000,000 tons of carbon dioxide of the annual discharging of Germany can be reduced half so.But, use the wait of still needing of this technology on a large scale.Will be in the power plant the about 20 billion cubic meter carbon dioxide of annual processing, need large quantities of bulk containers, the implementation and operation difficulty of getting up, manufacturing cost is than higher.
Japan's existing research on the fixing and treatment technology of carbon dioxide, as carbon dioxide catalyst immobilization technology, this technology is exactly by diverse ways such as catalytic hydrogenation, electrochemical reaction, photochemical fixation reaction, artificial photosynthesis, and carbon dioxide is changed into fuel or organic chemicals.But the enforcement difficulty of this technology is bigger, for the performance that how to improve catalyst, reaction efficiency and life-span, fine solution is not arranged also at present.Except above-mentioned technology, they also utilize vegetation stabilizing carbon dioxide technology, and in this technology, they utilize the photosynthesis stabilizing carbon dioxide of sea life or terrestrial plant.At present, Japan has begun to utilize little algae stabilizing carbon dioxide, carries out photosynthesis in open pond, because carbon dioxide is water-soluble slightly, and under zero degree and atmospheric pressure, solvable 1.79 volumes carbon dioxide of every volume, and generate weak acid.But along with temperature raises, carbon dioxide is overflowed in water.Though stir and utilize micro algae growth, also can quicken carbon dioxide and escape.Thereby the target that will reach high density and consume carbon dioxide efficiently, in a large number can't realize for now.So this technology must promotion and implementation, also need to break through guardian technique, as the high-density planting technology of algae and fast growing wood technology etc.
Therefore, from above-mentioned situation, at present should how to utilize problem fully at the carbon dioxide in the production of energy, though various countries have proposed some ways, but also there are some basic technical difficult problems, can not effectively a large amount of chemical recycling of carbon dioxide, turn waste into wealth, especially industrialized utilization is produced as the carbon dioxide of discarded object, also is unrealized at present.
Summary of the invention
Given this, the purpose of this utility model is to provide a kind of device that utilizes biological photo-synthetic reactor that carbon dioxide is used and change into oxygen, this installs low cost of manufacture, implement simple, trans-utilization is as the carbon dioxide of discarded object fully, turn waste into wealth, and can carry out suitability for industrialized production, the carbon dioxide of Xie Jueing is to the pollution of environment effectively.
In order to achieve the above object, the purpose of this utility model is achieved by the following technical solution:
This biology photo-synthetic reactor carbon dioxide reforming unit, it comprises that the carbon dioxide filtration desulfurizer, carbon dioxide gas storage tower, carbon dioxide jet flow-disturbing system, two circulating biological reaction tower, diode actinic light source control system, the temperature adjustment circulatory system, the oxygen that are connected with the CO2 emission source are collected tower, microorganism separates recovery system, plurality of conduits composition.Described carbon dioxide gas storage tower one end connects carbon dioxide by pipeline and filters desulfurizer, the other end connects carbon dioxide jet flow-disturbing system by pipeline, described pair of circulating biological reaction tower is to constitute by interior jar and outer jar, interior jar of inside at described pair of circulating biological reaction tower is equipped with carbon dioxide jet flow-disturbing system and diode actinic light source control system, outer pot bottom at two circulating biological reaction towers is equipped with the temperature adjustment circulatory system, described oxygen is collected tower and is passed through pipeline, air valve, the gas centrifugation pump is connected with the interior pot bottom of described pair of circulating biological reaction tower, and is connected with microorganism separation recovery system in interior jar of bottom of two circulating biological reaction towers by pipeline.
Described carbon dioxide jet flow-disturbing system is by air pump, nozzle disc, pipeline and plurality of nozzles are formed, described air pump is by pipeline and nozzle disc, nozzle is connected, nozzle is installed on the nozzle disc, and the bore of nozzle, angle, height and density right and wrong balanced distribution, can utilize the carbon dioxide gas stream that ejects to stir biologically active suspension in interior jar of two circulating biological reaction towers like this, form turbulence effect, biologically active suspension improves photosynthetic efficiency in turbulent flow, make microbial cell quicken division, in the microbial cell fission process, consume great amount of carbon dioxide, generate a large amount of oxygen.
Described actinic light source control system is made up of lamp and diode blood orange light source, orchid light source, described diode blood orange light source, orchid light source are the interior jar of inside that is installed in two circulating biological reaction towers by the regulation and control parameter, and, can under no natural daylight condition, effectively promote biological photosynthesis by photosensitive switch control.
The described temperature adjustment circulatory system is made up of temperature control water circulation tank, pipeline, liquid valve, circulating pump, two circulating biological reaction tower, the temperature control water circulation tank is connected with the outer pot bottom of two circulating biological reaction towers by pipeline, liquid valve, circulating pump, form an Inlet and outlet water circulation canal, the internally intensification of jar biological suspension system oxygen liquid and the effect of cooling effectively.
Described microorganism separates recovery system and is made up of circulatory pool, liquid valve, gas centrifugation pump, tube centrifuge, circulating pump, plurality of conduits, two circulating biological reaction tower, one end of described gas centrifugation pump passes through the interior pot bottom of pipeline, the two circulating biological reaction towers of liquid valve connection as the microbial liquid flow pass, and the other end of gas centrifugation pump connects the interior pot bottom of liquid valve, circulatory pool, liquid valve, tube centrifuge, circulating pump, liquid valve, two circulating biological reaction towers as the microbial liquid flow channel successively by pipeline again.
Jar and outer jar all are to be made by the rare-earth light-converting macromolecule transparent material in described.
The described pair of circulating biological reaction tower can be made up of two circulating biological reaction towers and be connected the temperature adjustment circulatory system and separate on the recovery system with microorganism, also can form a concatemer pair circulating biological reaction towers by a plurality of two circulating biological reaction towers side by side and be connected the temperature adjustment circulatory system and separate on the recovery system with microorganism.
The utlity model has following advantage: will change into oxygen fully as the carbon dioxide of discarded object by utilizing biological photo-synthetic reactor, the microbial suspension of producing simultaneously contains a large amount of active proteic substances, be splendid green liquid fertilizer or animal feed, turn waste into wealth, and can carry out suitability for industrialized production, consume carbon dioxide in large quantities, the carbon dioxide of Xie Jueing is to the pollution of environment effectively, this device low cost of manufacture is implemented simple.
Description of drawings
Fig. 1 is a structural representation of the present utility model;
Fig. 2 is a structural representation of being made of the two circulating biological reaction towers of a concatemer two two circulating biological reaction towers arranged side by side.
Fig. 3 is a structural representation of being made of the two circulating biological reaction towers of a concatemer three two circulating biological reaction towers arranged side by side.
The specific embodiment
The utility model is described in further detail below in conjunction with accompanying drawing:
As shown in Figure 1, steel plant, power plant, the carbon dioxide of CO2 emission sources such as oil plant 1 discharging filters desulfurizer 2 by the carbon dioxide that is connected with this CO2 emission source 1 and carries out desulfurization, after carbon dioxide after the desulfurization stores by carbon dioxide air accumulator 3 again, and then uniformly carbon dioxide is flowed in the carbon dioxide jet flow-disturbing system 8 of interior jar of 7 inside that are installed in two circulating biological reaction towers 5, this carbon dioxide jet flow-disturbing system 8 is by air pump 4, nozzle disc 10, pipeline 31 and plurality of nozzles 9 are formed, after carbon dioxide pressurizes by air pump 4, again by pipeline 31, from being installed in bore on the nozzle disc 10, angle, nozzle 9 ejections of height and density right and wrong balanced distribution, biologically active suspension in interior jar 7 of the two circulating biological reaction towers 5 of carbon dioxide gas stream stirring that eject, form turbulence effect, biologically active suspension improves photosynthetic efficiency in turbulent flow, make microbial cell quicken division, in the microbial cell fission process, consume great amount of carbon dioxide, generate a large amount of oxygen.Two circulating biological reaction towers 5 interior jars 7 in have a large amount of oxygen biological suspension system oxygen liquid by pipeline 31, air valve 28, gas centrifugation pump 19 with biological suspension system oxygen liquid and oxygen separation, oxygen after the separation is collected in the tower 13 by air valve 20 input oxygen, biological suspension system oxygen liquid enters in the circulatory pool 17 by liquid valve 18, after entering biological suspension system oxygen liquid in the circulatory pool 17 and organism being separated, enter in interior jar 7 of two circulating biological reaction towers 5 by circulating pump 14, liquid valve 29 again by liquid valve 16, tube centrifuge 15.
The intensification and the cooling of biological suspension system oxygen liquid are controlled by the temperature adjustment circulatory system 21 in interior jar 7 of two circulating biological reaction towers 5, the temperature adjustment circulatory system 21 is by temperature control water circulation tank 22, pipeline 31, liquid valve 23,24,27,30, circulating pump 25,26, two circulating biological reaction towers 5 are formed, water in the temperature control water circulation tank 22 is by pipeline 31, liquid valve 24, circulating pump 26, liquid valve 30 enters in the outer jar 6 of two circulating biological reaction towers 5, water in outer jar 6 of two circulating biological reaction towers 5 is again by pipeline 31, liquid valve 27, circulating pump 25, liquid valve 23 enters in the temperature control water circulation tank 22, form an Inlet and outlet water circulation canal like this, the internally intensification of jar biological suspension system oxygen liquid and the effect of cooling effectively.
Biological suspension system oxygen liquid is installed in interior jar of 7 internal body diodes blood orange light sources (wavelength 600-700nm), orchid light source (the wavelength 400-500nm) of two circulating biological reaction towers 5 in interior jar 7 of two circulating biological reaction towers 5 by the regulation and control parameter by photosensitive switch control, can under no natural daylight condition, effectively promote the biological photosynthesis of biological suspension system oxygen liquid, improve photosynthetic efficiency.
As shown in Figure 3, two circulating biological reaction towers can be formed the two circulating biological reaction towers of a concatemer by two two circulating biological reaction towers arranged side by side and are connected the temperature adjustment circulatory system and separate on the recovery system with microorganism.
As shown in Figure 4, two circulating biological reaction towers can be formed the two circulating biological reaction towers of a concatemer by three two circulating biological reaction towers arranged side by side and are connected the temperature adjustment circulatory system and separate on the recovery system with microorganism.
Claims (9)
1, a kind of biological photo-synthetic reactor carbon dioxide reforming unit, it is characterized in that: it comprises that the carbon dioxide that is connected with CO2 emission source (1) filters desulfurizer (2), carbon dioxide gas storage tower (3), carbon dioxide jet flow-disturbing system (8), two circulating biological reaction towers (5), diode actinic light source control system (11), the temperature adjustment circulatory system (21), oxygen is collected tower (13), microorganism separates recovery system (12), plurality of conduits (31) is formed, described carbon dioxide gas storage tower (3) one ends connect carbon dioxide by pipeline (31) and filter desulfurizer (2), the other end connects carbon dioxide jet flow-disturbing system (8) by pipeline (31), described pair of circulating biological reaction tower (5) is to be made of interior jar (7) and outer jar (6), interior jar of (7) inside at described pair of circulating biological reaction tower (5) is equipped with carbon dioxide jet flow-disturbing system (8) and diode actinic light source control system (11), outer jar (6) bottom at two circulating biological reaction towers (5) is equipped with the temperature adjustment circulatory system (21), described oxygen is collected tower (13) by pipeline (31), air valve (20), gas centrifugation pump (19) is connected with interior jar (7) bottom of described pair of circulating biological reaction tower (5), and is connected with microorganism separation recovery system (12) in interior jar of (7) bottom of two circulating biological reaction towers (5) by pipeline (31).
2, biological photo-synthetic reactor carbon dioxide reforming unit according to claim 1, it is characterized in that: described carbon dioxide jet flow-disturbing system (8) is made up of air pump (4), nozzle disc (10), pipeline (31) and plurality of nozzles (9), and described air pump is connected with nozzle disc (10), nozzle (9) by pipeline (31).
3, biological photo-synthetic reactor carbon dioxide reforming unit according to claim 1, it is characterized in that: described diode actinic light source control system (11) is made up of lamp and diode blood orange light source, orchid light source.
4, biological photo-synthetic reactor carbon dioxide reforming unit according to claim 1, it is characterized in that: the described temperature adjustment circulatory system (21) is by temperature control water circulation tank (22), pipeline (31), liquid valve (23,24,27,30), circulating pump (25,26), two circulating biological reaction towers (5) are formed, temperature control water circulation tank (22) is by pipeline (31), liquid valve (23,24,27,30), circulating pump (25,26) be connected with outer jar (6) bottom of two circulating biological reaction towers (5), form an Inlet and outlet water circulation canal, the internally intensification of jar biological suspension system oxygen liquid and the effect of cooling effectively.
5, biological photo-synthetic reactor carbon dioxide reforming unit according to claim 1, it is characterized in that: it is by circulatory pool (17) that described microorganism separates recovery system (12), liquid valve (16,18,28,29), gas centrifugation pump (19), tube centrifuge (15), circulating pump (14), plurality of conduits (31), two circulating biological reaction towers (5) are formed, one end of described gas centrifugation pump (19) is by pipeline (31), liquid valve (28) connects interior jar (7) bottom of two circulating biological reaction towers (5) as the microbial liquid flow pass, and the other end of gas centrifugation pump (19) connects liquid valve (18) successively by pipeline (31) again, circulatory pool (17), liquid valve (16), tube centrifuge (15), circulating pump (14), liquid valve (29), interior jar (7) bottom of two circulating biological reaction towers (5) is as the microbial liquid flow channel.
6, biological photo-synthetic reactor carbon dioxide reforming unit according to claim 1 is characterized in that: jar (7) and outer jar (6) all are to be made by the rare-earth light-converting macromolecule transparent material in described.
7, biological photo-synthetic reactor carbon dioxide reforming unit according to claim 1, it is characterized in that: described pair of circulating biological reaction tower (5) can be made up of two circulating biological reaction towers and be connected the temperature adjustment circulatory system (21) and separate with microorganism on the recovery system (12), also can form a concatemer pair circulating biological reaction towers (5) by a plurality of two circulating biological reaction towers (5) side by side and be connected the temperature adjustment circulatory system (21) and separate with microorganism on the recovery system (12).
8, biological photo-synthetic reactor carbon dioxide reforming unit according to claim 2, it is characterized in that: described nozzle (9) is installed on the nozzle disc (10), and the bore of nozzle, angle, height and density right and wrong balanced distribution.
9, biological photo-synthetic reactor carbon dioxide reforming unit according to claim 3, it is characterized in that: described diode blood orange light source, orchid light source are interior jar of (7) inside that is installed in two circulating biological reaction towers (5) by the regulation and control parameter, and control by photosensitive switch.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNU2006200228659U CN2885390Y (en) | 2006-03-29 | 2006-03-29 | Carbon dioxide conversion device for biological photosynthesis reactor |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNU2006200228659U CN2885390Y (en) | 2006-03-29 | 2006-03-29 | Carbon dioxide conversion device for biological photosynthesis reactor |
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| Publication Number | Publication Date |
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| CN2885390Y true CN2885390Y (en) | 2007-04-04 |
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| Application Number | Title | Priority Date | Filing Date |
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| CNU2006200228659U Expired - Fee Related CN2885390Y (en) | 2006-03-29 | 2006-03-29 | Carbon dioxide conversion device for biological photosynthesis reactor |
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Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102292140A (en) * | 2009-01-20 | 2011-12-21 | 国家农业研究院 | Method for the fixation of co2 and for treating organic waste by coupling an anaerobic digestion system and a phytoplankton microorganism production system |
| CN111437716A (en) * | 2020-04-03 | 2020-07-24 | 北京航空航天大学 | Microalgae carbon sequestration method based on natural environment regulation |
-
2006
- 2006-03-29 CN CNU2006200228659U patent/CN2885390Y/en not_active Expired - Fee Related
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102292140A (en) * | 2009-01-20 | 2011-12-21 | 国家农业研究院 | Method for the fixation of co2 and for treating organic waste by coupling an anaerobic digestion system and a phytoplankton microorganism production system |
| CN111437716A (en) * | 2020-04-03 | 2020-07-24 | 北京航空航天大学 | Microalgae carbon sequestration method based on natural environment regulation |
| CN111437716B (en) * | 2020-04-03 | 2021-11-26 | 北京航空航天大学 | Microalgae carbon sequestration method based on natural environment regulation |
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Owner name: BEIJING GREEN SUN BIOLOGICAL ENGINEERING TECHNOLOG Free format text: FORMER OWNER: ZHANG ZHANGQING Effective date: 20100520 Free format text: FORMER OWNER: TIAN YUZHAO |
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Free format text: CORRECT: ADDRESS; FROM: 100091 ROOM 302, BUILDING 15, GUYUEYUAN, TIANXIU GARDEN, TIANXIU ROAD, HAIDIAN DISTRICT, BEIJING TO: 100085 602, TOWER B, INTERNATIONAL VENTURE PARK, NO.1 XINXI ROAD, SHANGDI, HAIDIAN DISTRICT, BEIJING |
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Effective date of registration: 20100520 Address after: 100085, B, block 1, international pioneer park, 602 information road, Beijing, Haidian District Patentee after: Beijing Luyuan photosynthetic Biological Engineering Technology Co Ltd Address before: Beijing City, Haidian District road 100091 days show garden Gu Yue application of Raman spectroscopy in cancer diagnosis Park building 15, Room 302 Co-patentee before: Tian Yuzhao Patentee before: Zhang Changqing |
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Owner name: BEIJING ZHONGQI GUOYUN ENTERPRISE MANAGEMENT CONSU Free format text: FORMER OWNER: BEIJING GREEN SUN BIOLOGICAL ENGINEERING TECHNOLOGY CO., LTD. Effective date: 20120424 |
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