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CN101766955A - System and method for reducing carbon dioxide using photosynthetic reaction device - Google Patents

System and method for reducing carbon dioxide using photosynthetic reaction device Download PDF

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CN101766955A
CN101766955A CN200810192993A CN200810192993A CN101766955A CN 101766955 A CN101766955 A CN 101766955A CN 200810192993 A CN200810192993 A CN 200810192993A CN 200810192993 A CN200810192993 A CN 200810192993A CN 101766955 A CN101766955 A CN 101766955A
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carbon dioxide
photosynthetic reaction
reaction device
algae
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卢朝辉
卢星宏
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Abstract

一种利用光合反应装置以减少二氧化碳的系统和方法,所述系统包括一二氧化碳产生系统及一藻类生产设备,二氧化碳产生系统包含一产生二氧化碳的锅炉,藻类生产设备包含一与锅炉连通的涤气处理器及多个与涤气处理器连通的藻类光合反应装置;由前述,借由藻类生产设备而能将二氧化碳产生系统所排放出二氧化碳收集再利用,以达到减少二氧化碳排出于大气中的目的。

Figure 200810192993

A system and method for reducing carbon dioxide using a photosynthetic reaction device, the system comprising a carbon dioxide generating system and an algae production device, the carbon dioxide generating system comprising a boiler for generating carbon dioxide, the algae production device comprising a gas scrubber connected to the boiler and a plurality of algae photosynthetic reaction devices connected to the gas scrubber; based on the foregoing, the carbon dioxide emitted by the carbon dioxide generating system can be collected and reused by means of the algae production device, so as to achieve the purpose of reducing the emission of carbon dioxide into the atmosphere.

Figure 200810192993

Description

利用光合反应装置以减少二氧化碳的系统及方法 System and method for reducing carbon dioxide using photosynthetic reaction device

技术领域technical field

本发明涉及一种光合反应装置,尤指一种利用光合反应装置以减少二氧化碳的系统及方法。The invention relates to a photosynthetic reaction device, in particular to a system and method for reducing carbon dioxide by using the photosynthetic reaction device.

背景技术Background technique

人类文明的发展,带来舒适环境与物质上的享受,但随着工业发展,从火力发电厂、垃圾焚化炉、化工厂、汽机车等所排放至大气中的二氧化碳(CO2)不断的增加,而二氧化碳所造成的“温室效应”已成为地球温暖化的原因,因而需要尽快地节省排出二氧化碳的排出量,以防止温室效应的恶化。The development of human civilization brings a comfortable environment and material enjoyment, but with the development of industry, the carbon dioxide (CO 2 ) emitted into the atmosphere from thermal power plants, garbage incinerators, chemical plants, automobiles, etc. continues to increase , and the "greenhouse effect" caused by carbon dioxide has become the cause of global warming, so it is necessary to save the amount of carbon dioxide emitted as soon as possible to prevent the deterioration of the greenhouse effect.

如以火力发电厂为例,其锅炉燃烧石油燃料、煤炭燃料、LNG(液化天然气)等燃料时,即产生出大量的二氧化碳,其必须经过处理或收集再利用,否则大量排放至大气中,则使温室效应的情况更加恶化,故如何有效节省排出二氧化碳、分离二氧化碳或将排出的二氧化碳收集再利用,已成为目前环保议题上相当重要的课题之一。Take a thermal power plant as an example, when its boiler burns petroleum fuel, coal fuel, LNG (liquefied natural gas) and other fuels, it will produce a large amount of carbon dioxide, which must be treated or collected for reuse, otherwise it will be discharged into the atmosphere in large quantities, then The situation of the greenhouse effect is worsened, so how to effectively save carbon dioxide, separate carbon dioxide or collect and reuse the discharged carbon dioxide has become one of the most important issues in environmental protection issues.

发明内容Contents of the invention

本发明的主要目的,是提出一种利用光合反应装置以减少二氧化碳的系统及方法,借以将排放出的二氧化碳收集再利用,以达到减少二氧化碳排出于大气中的目的。The main purpose of the present invention is to provide a system and method for reducing carbon dioxide by using a photosynthetic reaction device, so as to collect and reuse the emitted carbon dioxide, so as to reduce the emission of carbon dioxide into the atmosphere.

本发明的次一目的,在于提出一种利用光合反应装置以减少二氧化碳的系统及方法,使光合反应装置所生产出的藻类具有经济价值而可制成保健品、食用品或提炼出油品等。The second purpose of the present invention is to propose a system and method for reducing carbon dioxide by using a photosynthetic reaction device, so that the algae produced by the photosynthetic reaction device have economic value and can be made into health care products, edible products or oil products, etc. .

本发明的另一目,在于提出一种利用光合反应装置以减少二氧化碳的系统及方法,其光合反应装置具有所需占地面积小、能源使用减少、运转不受天候的影响等效用,能避免受污染以维护所产生藻类的质量。Another object of the present invention is to propose a system and method for reducing carbon dioxide by using a photosynthetic reaction device. Pollution to maintain the quality of the algae produced.

依据上述目的,本发明提出一种利用光合反应装置以减少二氧化碳的系统,包括:一二氧化碳(CO2)产生系统,其包含有一产生二氧化碳的锅炉;以及一藻类生产设备,其包含一与该锅炉连通的涤气处理器及多个与该涤气处理器连通的藻类光合反应装置,每一藻类光合反应装置包括:一光合反应单元,其为透光管路;一加压输液单元,其与该透光管路连通,该加压输液单元具有一输液管;一喷射排氧单元,其为中空筒件而具有相组接的一排氧筒与一集液筒,该排氧筒设有一进液口、一上排气口和一中空管壁,该进液口连通于该输液管的出口端,该上排气口位于该排氧筒的顶端,该中空管壁自该上排气口向下延伸;一连通管体,其连通该集液筒及该透光管路;以及一输气管,其一端与该涤气处理器连通,另一端伸入至该集液筒内。According to the above purpose, the present invention proposes a system for reducing carbon dioxide by using a photosynthetic reaction device, including: a carbon dioxide (CO 2 ) generation system, which includes a boiler for generating carbon dioxide; and an algae production device, which includes a A connected scrubber and a plurality of algae photosynthetic reaction devices connected with the scrubber, each algae photosynthetic reaction device includes: a photosynthetic reaction unit, which is a light-transmitting pipeline; a pressurized infusion unit, which is connected with the The light-transmitting pipeline is connected, and the pressurized infusion unit has an infusion tube; a jet oxygen exhaust unit, which is a hollow cylinder and has an oxygen exhaust cylinder and a liquid collection cylinder assembled together, and the oxygen exhaust cylinder is provided with a A liquid inlet, an upper exhaust port and a hollow pipe wall, the liquid inlet is connected to the outlet end of the infusion tube, the upper exhaust port is located at the top of the oxygen exhaust cylinder, and the hollow pipe wall is exhausted from the upper The mouth extends downward; a connecting pipe body, which communicates with the liquid collecting cylinder and the light-transmitting pipeline; and an air delivery pipe, one end of which communicates with the scrubber, and the other end extends into the liquid collecting cylinder.

为达上述目的,本发明并提出一种利用光合反应装置以减少二氧化碳的方法,利用上述利用光合反应装置以减少二氧化碳的系统,该方法包括:In order to achieve the above object, the present invention also proposes a method for reducing carbon dioxide by utilizing a photosynthetic reaction device, using the above-mentioned system for reducing carbon dioxide by utilizing a photosynthetic reaction device, the method comprising:

该二氧化碳产生系统的锅炉经燃料燃烧后而产生二氧化碳;the boiler of the carbon dioxide generating system produces carbon dioxide through the combustion of fuel;

上述的二氧化碳引入至该藻类生产设备的涤气处理器,以净化该二氧化碳;The above-mentioned carbon dioxide is introduced into the scrubber of the algae production equipment to purify the carbon dioxide;

该等藻类光合反应装置的透光管路内分别注入有藻类及微生物的培养液,该培养液流动于该透光管路内以进行光合作用且生成氧气,该培养液并流向该加压输液单元;The light-transmitting pipelines of these algae photosynthetic reaction devices are respectively injected with culture fluids of algae and microorganisms, and the culture fluid flows in the light-transmitting pipelines to perform photosynthesis and generate oxygen, and the culture fluid flows to the pressurized infusion fluid unit;

上述的加压输液单元强迫该培养液由该输液管进入至该喷射排氧单元,使该培养液冲击于该排氧筒内,以形成一旋转水花扩散飞溅状自该上排气口排出氧气,该培养液落下收集于该集液筒;The above-mentioned pressurized infusion unit forces the culture solution to enter the spray oxygen exhaust unit from the infusion tube, so that the culture solution impacts in the oxygen exhaust cylinder to form a rotating water splash to discharge oxygen from the upper exhaust port. , the culture solution falls and is collected in the collection tube;

上述的二氧化碳由该输气管导入于该集液筒内的培养液中,使该培养液的藻类吸收该二氧化碳;以及The above-mentioned carbon dioxide is introduced into the culture solution in the liquid collection tube through the gas delivery pipe, so that the algae in the culture solution can absorb the carbon dioxide; and

上述的培养液由该连通管体再流入至该透光管路内,以再次进行光合作用而生成氧气。The above-mentioned culture solution flows into the light-transmitting pipeline through the connecting pipe body, so as to perform photosynthesis again to generate oxygen.

本发明具有的优点:The advantages that the present invention has:

1、借由藻类生产设备与二氧化碳产生系统相结合,借以可将排放出的二氧化碳收集再利用,以达到减少二氧化碳排出于大气中的目的。1. By combining the algae production equipment with the carbon dioxide generation system, the emitted carbon dioxide can be collected and reused, so as to reduce the emission of carbon dioxide into the atmosphere.

2、藻类生产设备的每一藻类光合反应装置所生产出的藻类具有经济价值而可制成保健品、食用品或提炼出油品等。2. The algae produced by each algae photosynthetic reaction device of the algae production equipment has economic value and can be made into health care products, edible products or refined oil products.

3、每一藻类光合反应装置借由透光管路、加压输液单元、喷射排氧单元及连通管体的连接组成,使注入于其内的培养液能够呈垂直立体多排管道密封循环地进行光合作用和排氧及吸收二氧化碳,具有所需占地面积减小、能源使用减少、运转不受天候的影响,能避免受污染以维护所产生藻类的质量,故可大量化建设于发力发电厂适当场所。3. Each algae photosynthetic reaction device is composed of a light-transmitting pipeline, a pressurized infusion unit, a jet oxygen exhaust unit and a connecting pipe body, so that the culture solution injected into it can be sealed and circulated in a vertical three-dimensional multi-row pipeline. Carrying out photosynthesis, deoxygenation and absorbing carbon dioxide, it has the advantages of reducing the required land area, reducing energy consumption, operation is not affected by the weather, and can avoid pollution to maintain the quality of the algae produced, so it can be built in large quantities. Suitable location for power plant.

4、每一藻类光合反应装置的排氧筒和集液筒的组接,及透光管路的设计,使得每一藻类光合反应装置易于清洗、维护,以确保光合作用的效果和藻类的质量。4. The assembly of the oxygen exhaust cylinder and the liquid collection cylinder of each algae photosynthetic reaction device, and the design of the light-transmitting pipeline make each algae photosynthetic reaction device easy to clean and maintain, so as to ensure the effect of photosynthesis and the quality of algae .

为了能更进一步了解本发明为达到既定目的所采取的技术、方法及技术效果,请参阅有关本发明的详细说明与附图,相信本发明的目的、特征与特点,当可由此得一深入且具体的了解,然而所附附图仅提供参考与说明用,并非用来对本发明加以限制。In order to further understand the technology, method and technical effect that the present invention takes to achieve the intended purpose, please refer to the detailed description and accompanying drawings of the present invention. It is believed that the purpose, characteristics and characteristics of the present invention can be obtained from this For specific understanding, however, the accompanying drawings are only for reference and illustration, and are not intended to limit the present invention.

附图说明Description of drawings

图1为本发明利用光合反应装置以减少二氧化碳的系统的示意图。FIG. 1 is a schematic diagram of a system for reducing carbon dioxide by using a photosynthetic reaction device according to the present invention.

图2为本发明中的藻类光合反应装置的示意图(一)。Fig. 2 is a schematic diagram (1) of the algae photosynthetic reaction device in the present invention.

图3为本发明中的藻类光合反应装置的示意图(二)。Fig. 3 is a schematic diagram (2) of the algae photosynthetic reaction device in the present invention.

图4为本发明中的藻类光合反应装置的示意图(三)。Fig. 4 is a schematic diagram (3) of the algae photosynthetic reaction device in the present invention.

图5为本发明中的藻类光合反应装置的示意图(四)。Fig. 5 is a schematic diagram (four) of the algae photosynthetic reaction device in the present invention.

图6为本发明中的藻类光合反应装置的示意图(五)。Fig. 6 is a schematic diagram (5) of the algae photosynthetic reaction device in the present invention.

图7为本发明中的藻类光合反应装置的示意图(六)。Fig. 7 is a schematic diagram (6) of the algae photosynthetic reaction device in the present invention.

图8为本发明中的藻类光合反应装置的示意图(七)。Fig. 8 is a schematic diagram (7) of the algae photosynthetic reaction device in the present invention.

图9为本发明利用光合反应装置以减少二氧化碳的方法的流程图。FIG. 9 is a flowchart of a method for reducing carbon dioxide by using a photosynthetic reaction device according to the present invention.

【主要元件附图标记说明】[Description of reference signs of main components]

二氧化碳产生系统100Carbon dioxide generation system 100

锅炉11                加热处理器12Boiler 11 Heating Processor 12

涡轮机13              发电机14Turbine 13 Generator 14

冷却处理器15          冷凝管路151Cooling processor 15 Condensing pipeline 151

回流管16              汽水分离器17Return pipe 16 Steam-water separator 17

藻类生产设备200Algae production equipment 200

涤气处理器21          温变调控器22Scrubbing processor 21 Temperature regulator 22

流量控制器23          引导管24Flow controller 23 Guide pipe 24

藻类光合反应装置3Algae Photosynthetic Reactor 3

光合反应单元31Photosynthetic Reaction Unit 31

直管311               弯管312Straight pipe 311 Bend pipe 312

辅助开口313Auxiliary opening 313

加压输液单元32Pressurized infusion unit 32

输液管321Infusion tube 321

喷射排氧单元33Jet exhaust unit 33

排氧筒331Oxygen cylinder 331

进液口3311            上排气口3312Liquid inlet 3311 Upper exhaust port 3312

缩颈部3313            侧排气口3314Neck 3313 side exhaust port 3314

集液筒332Liquid collection cylinder 332

中空管壁333Hollow tube wall 333

排气管334exhaust pipe 334

扩张部3341Expansion 3341

连通管体34Connecting pipe body 34

输气管35Air pipe 35

采收阀组件36Recovery Valve Assembly 36

连通单元37Connectivity Unit 37

温度调控单元38Temperature control unit 38

加/降温管381         入口转接部382Adding/cooling pipe 381 Inlet adapter 382

出口转接部383Export transfer section 383

连通管路件39Connecting pipeline parts 39

开关阀组件391Switch valve assembly 391

洒水单元40sprinkler unit 40

补光单元41Fill light unit 41

调节筒体42Regulating cylinder 42

接管43Take over 43

排气单元44exhaust unit 44

排气集液筒441        第一通管442Exhaust liquid collection cylinder 441 First pipe 442

第二通管443Second through pipe 443

具体实施方式Detailed ways

请先参阅图1,本发明提出一种利用光合反应装置以减少二氧化碳的系统,其包括有一二氧化碳(CO2)产生系统100及一藻类生产设备200。Please refer to FIG. 1 first. The present invention proposes a system for reducing carbon dioxide by using a photosynthetic reaction device, which includes a carbon dioxide (CO 2 ) generation system 100 and an algae production device 200 .

首先,先说明二氧化碳产生系统100,其主要需包含有一产生二氧化碳的锅炉11,因此,在本发明中二氧化碳产生系统100为一占地广大的火力发电厂,且通常是处于近水域附近,而更包含有一加热处理器12、一涡轮机13、一发电机14、一冷却处理器15、一回流管16及一汽水分离器17。汽水分离器17与锅炉11连通,加热处理器12与汽水分离器17连通、涡轮机13与加热处理器12连通、发电机14则与涡轮机13同轴向的连结,而冷却处理器15与涡轮机13相连通,冷却处理器15即与回流管16连通。First of all, the carbon dioxide generation system 100 will be described first, which mainly needs to include a boiler 11 for generating carbon dioxide. Therefore, in the present invention, the carbon dioxide generation system 100 is a thermal power plant that occupies a large area, and is usually near waters, and more It includes a heating processor 12 , a turbine 13 , a generator 14 , a cooling processor 15 , a return pipe 16 and a steam-water separator 17 . The steam-water separator 17 communicates with the boiler 11, the heating processor 12 communicates with the steam-water separator 17, the turbine 13 communicates with the heating processor 12, the generator 14 is connected with the turbine 13 coaxially, and the cooling processor 15 communicates with the turbine 13 The cooling processor 15 communicates with the return pipe 16 .

接着,大致说明上述系统的作动,锅炉11引入水后,再经燃料燃烧后即产生蒸汽及二氧化碳,其中蒸汽随即被引导至汽水分离器17,而分离含于蒸汽中的水汽,分离出的水汽可经由凝结成水后而再引回锅炉11内,分离后的蒸汽即被引导至加热处理器12,以再加热蒸汽而再升高其温度,使成为高温高压的蒸汽;之后,加热至高温高压的蒸汽即进入至涡轮机13内,进而驱动涡轮机13的叶片产生转动以驱动发电机14发电,使用过后的蒸汽借由冷却处理器15具有的冷凝管路151左侧所引入的海水或河水冷却而使用过后的水再由右侧流回海水或河水,冷却处理器15管中的蒸汽即可冷凝转成热水而经由回流管16可再回流至锅炉11内。Next, the operation of the above-mentioned system will be roughly described. After the boiler 11 introduces water, steam and carbon dioxide will be generated after the fuel is burned, and the steam will be led to the steam-water separator 17 to separate the water vapor contained in the steam. The water vapor can be condensed into water and then lead back into the boiler 11, and the separated steam is led to the heating processor 12 to reheat the steam to raise its temperature again, so that it becomes high-temperature and high-pressure steam; after that, it is heated to The high-temperature and high-pressure steam enters the turbine 13, and then drives the blades of the turbine 13 to rotate to drive the generator 14 to generate electricity. The used steam cools the seawater or river water introduced from the left side of the condensing pipeline 151 of the processor 15. The cooled and used water flows back to sea water or river water from the right side, and the steam in the cooling processor 15 tube can be condensed and turned into hot water, which can then flow back into the boiler 11 through the return pipe 16 .

接着,说明上述的藻类生产设备200,其包含一涤气处理器21及多个藻类光合反应装置3;涤气处理器21与锅炉11连通,每一藻类光合反应装置3与涤气处理器21连通,且可设置于适当场所处,如建筑物的顶楼、具屋檐的半封闭空间等,另外,值得一提的是,前述的连通如锅炉11与涤气处理器21等可借由导管而使前述的构件相互连通,及藻类光合反应装置3的数量乃依据火力发电厂规模及所排放出二氧化碳的单位而设置,故有可能是为数百个,或是高达上千以上的数量不等。Then, the above-mentioned algae production equipment 200 is described, which includes a scrubber 21 and a plurality of algae photosynthetic reaction devices 3; connected, and can be installed in a suitable place, such as the top floor of a building, a semi-enclosed space with eaves, etc. In addition, it is worth mentioning that the aforementioned connections such as the boiler 11 and the scrubber 21 can be connected through conduits The aforementioned components are connected to each other, and the number of algae photosynthetic reaction devices 3 is set according to the scale of the thermal power plant and the unit of carbon dioxide emitted, so there may be hundreds, or up to thousands or more. .

请再搭配图2所示,每一藻类光合反应装置3包括有一光合反应单元31、一加压输液单元32、一喷射排氧单元33、一连通管体34及一输气管35。As shown in FIG. 2 , each algae photosynthetic reaction device 3 includes a photosynthetic reaction unit 31 , a pressurized infusion unit 32 , a spray oxygen exhaust unit 33 , a connecting pipe body 34 and an air pipe 35 .

上述光合反应单元31为一透光管路,其可包括多个直管311和多个弯管312,该等直管311和该等弯管312间隔串接形成一双排倾斜的立体盘旋式透光管路,且透光管路的最上方部份更设有一辅助开口313。The above-mentioned photosynthetic reaction unit 31 is a light-transmitting pipeline, which may include a plurality of straight pipes 311 and a plurality of curved pipes 312, and the straight pipes 311 and the curved pipes 312 are connected in series at intervals to form a double row of inclined three-dimensional spiral transparent pipes. The light pipe is further provided with an auxiliary opening 313 at the uppermost part of the light-transmitting pipe.

加压输液单元32为一加压输液泵,其与上述透光管路连通,且具有一输液管321。The pressurized infusion unit 32 is a pressurized infusion pump, which communicates with the above-mentioned transparent pipeline and has an infusion tube 321 .

喷射排氧单元33为中空筒件,且具有上下相组接的一排氧筒331与一集液筒332,排氧筒331的上段设有一进液口3311、一上排气口3312和一中空管壁333,进液口3311与加压输液单元32的输液管321的出口端连通。上排气口3312位于排氧筒331的顶端,中空管壁333自上排气口3312向下延伸而成。另,该排氧筒331的中段设有一缩颈部3313和一侧排气口3314,侧排气口3314位于缩颈部3313的下方。另一方面,喷射排氧单元33可再进一步包括一排气管334,其组接于排氧筒331内,排气管334的上端穿设于该中空管壁333内,且排气管334的下端可进一步地形成一扩张部3341且相对地位于侧排气口3314的内侧。The spray oxygen exhaust unit 33 is a hollow cylinder, and has an oxygen exhaust cylinder 331 and a liquid collection cylinder 332 assembled up and down. The hollow tube wall 333 and the liquid inlet 3311 communicate with the outlet end of the infusion tube 321 of the pressurized infusion unit 32 . The upper exhaust port 3312 is located at the top of the oxygen exhaust cylinder 331 , and the hollow tube wall 333 extends downward from the upper exhaust port 3312 . In addition, the middle section of the oxygen exhaust cylinder 331 is provided with a constricted portion 3313 and a side exhaust port 3314 , and the side exhaust port 3314 is located below the constricted portion 3313 . On the other hand, the spray oxygen exhaust unit 33 can further include an exhaust pipe 334, which is assembled in the oxygen exhaust cylinder 331, the upper end of the exhaust pipe 334 is penetrated in the hollow pipe wall 333, and the exhaust pipe 334 The lower end of the can further form an expansion portion 3341 and is relatively located inside the side exhaust port 3314 .

连通管体34为一两端为开口状的封闭式管路件而连通集液筒332及透光管路,而连通管体34可为一扩张管。The connecting pipe body 34 is a closed pipe member with openings at both ends to communicate with the liquid collection cylinder 332 and the light-transmitting pipe, and the connecting pipe body 34 can be an expansion pipe.

输气管35的一端与上述涤气处理器21连通,另一端则伸入至喷射排氧单元33的集液筒332内。One end of the gas delivery pipe 35 communicates with the above-mentioned scrubber 21 , and the other end extends into the liquid collection cylinder 332 of the jet oxygen exhaust unit 33 .

另外,本发明的每一藻类光合反应装置3更包括有一采收阀组件36,连通于透光管路的出口端与加压输液单元32的入口端间。In addition, each algae photosynthetic reaction device 3 of the present invention further includes a harvesting valve assembly 36 connected between the outlet end of the light-transmitting pipeline and the inlet end of the pressurized infusion unit 32 .

说明上述藻类生产设备200的运作,上述锅炉11所产生的二氧化碳可导引至涤气处理器21,其可去除混杂于二氧化碳中的有害元素,如硫、磷等。To illustrate the operation of the above-mentioned algae production equipment 200, the carbon dioxide produced by the above-mentioned boiler 11 can be guided to the scrubber 21, which can remove harmful elements mixed in the carbon dioxide, such as sulfur and phosphorus.

上述每一藻类光合反应装置3的透光管路的辅助开口313可供注入一藻类微生物藻种(藻类)及培养藻类微生物(微生物)的培养液(以下统称培养液)于透光管路内,该培养液与流动于该透光管路内并进行光合作用产生氧气,之后,该培养液并可流向加压输液单元32,进而开启加压输液单元32以强迫培养液自输液管321流入喷射排氧单元33。The auxiliary opening 313 of the light-transmitting pipeline of each of the above-mentioned algae photosynthetic reaction devices 3 can be used to inject an algae microorganism algae (algae) and a culture solution (hereinafter collectively referred to as culture fluid) for cultivating algae microorganisms (microorganisms) in the light-transmitting pipeline , the culture solution flows in the light-transmitting pipeline and undergoes photosynthesis to generate oxygen, and then the culture solution can flow to the pressurized infusion unit 32, and then the pressurized infusion unit 32 is opened to force the culture solution to flow from the infusion tube 321 Jet oxygen exhaust unit 33.

当培养液经由进液口3311喷射于排氧筒331内时,培养液首先冲击于喷射排氧单元33的排氧筒331内以形成一旋转水花状以利于氧气自上排气口3312排出;接着,培养液落下收集至缩颈部3313后冲击排气管334的扩张部3341而形成一扩散飞溅状,以利于氧气自该侧排气口3314排出;最后,该培养液落下收集于该集液筒332内,使氧气自该排气管334的上端排出;如此,可把大部分的氧气排出,此时,经由输气管35即可将上述的二氧化碳导入于集液筒332内的培养液中,因而使藻类能吸收二氧化碳,以提升该培养液再光合作用的能力,借以达到可加以收集而再利用上述发力发电厂所产生的二氧化碳,而达节排二氧化碳于大气中。When the culture solution is sprayed into the oxygen discharge cylinder 331 through the liquid inlet 3311, the culture solution first impacts into the oxygen discharge cylinder 331 of the injection oxygen discharge unit 33 to form a rotating spray shape to facilitate the discharge of oxygen from the upper exhaust port 3312; Then, the culture solution falls and collects to the constricted part 3313 and then impacts the expansion part 3341 of the exhaust pipe 334 to form a diffuse splash shape, so as to facilitate the discharge of oxygen from the side exhaust port 3314; finally, the culture solution falls and collects in the set. In the liquid cylinder 332, make oxygen discharge from the upper end of this exhaust pipe 334; Therefore, the algae can absorb carbon dioxide to enhance the ability of the culture medium to photosynthesize, so that the carbon dioxide produced by the above-mentioned power plant can be collected and reused, so as to save carbon dioxide in the atmosphere.

又,当集液筒332所收集的培养液的液面高度高于透光管路的最上层,而利用势能差产生压力,使培养液由连通管体34自动流入该透光管路内,从而再次进行光合作用,如此,该培养液即可于本发明的藻类光合反应装置3中反复循环培养以使藻类微生物逐渐繁殖,待该培养液中的藻类微生物含量达到可采收的程度时,即可开启采收阀组件36以进行采收。Also, when the liquid level of the culture solution collected by the liquid collection tube 332 is higher than the uppermost layer of the light-transmitting pipeline, the potential energy difference is used to generate pressure, so that the culture solution automatically flows into the light-transmitting pipeline through the connecting pipe body 34, Thereby carry out photosynthesis again, like this, this nutrient solution can be in the algal photosynthetic reaction device 3 of the present invention and repeatedly circulate and cultivate so that algae microorganisms multiply gradually, when the algae microorganism content in this nutrient solution reaches the degree that can be harvested, The recovery valve assembly 36 can then be opened for recovery.

而在藻类培养的过程中,该培养液流入该连通管体34时,由于该连通管体34为扩张管,因此该培养液的流速可在此处大幅减缓,使得培养液由扩张管流入该透光管路需要较长的时间,而使得该培养液中的藻类微生物有足够的时间可以在连通管体34进行生理调节的目的,以消除加压输液单元32以及喷射排氧单元33的作用所带来的生理伤害,而得以最佳的生理状态进入该透光管路,也因此能够采收到最佳质量的藻类,如蓝藻、红球藻或油藻等。In the process of algae cultivation, when the culture solution flows into the connecting pipe body 34, since the connecting pipe body 34 is an expansion tube, the flow velocity of the culture solution can be greatly slowed down here, so that the culture solution flows into the connecting pipe body 34 from the expansion pipe. The light-transmitting pipeline takes a long time, so that the algae microorganisms in the culture solution have enough time to perform physiological adjustment in the connecting pipe body 34, so as to eliminate the effects of the pressurized infusion unit 32 and the jet oxygen exhaust unit 33 The physiological damage caused can enter the light-transmitting pipeline in the best physiological state, and therefore the best quality algae, such as cyanobacteria, haematococcus or oil algae, can be harvested.

另,本发明的藻类生产设备200更可进一步包括温变调控器22及一流量控制器23,温变调控器22可连通于涤气处理器21之后与该等藻类光合反应装置3之间,用以使二氧化碳的降温,流量控制器23可连结于涤气处理器21与该等藻类光合反应装置3之间,而每一藻类光合反应装置3的输气管35与流量控制器23连通或连接,用以控制二氧化碳进入至每一藻类光合反应装置3的流量,但不以此为限,流量控制器23也可设置有多个而分别设置于输气管35上,借以达到控制二氧化碳进入至藻类光合反应装置3的流量;其中,流量控制器23可为一流量控制阀,或任何等效的构件皆可。In addition, the algae production equipment 200 of the present invention may further include a temperature change controller 22 and a flow controller 23, the temperature change controller 22 may be connected between the scrubber 21 and the algae photosynthetic reaction devices 3, In order to lower the temperature of carbon dioxide, the flow controller 23 can be connected between the scrubber 21 and the algae photosynthetic reaction devices 3, and the gas delivery pipe 35 of each algae photosynthetic reaction device 3 is communicated or connected to the flow controller 23 , used to control the flow of carbon dioxide into each algae photosynthetic reaction device 3, but not limited thereto, the flow controller 23 can also be provided with multiple and respectively arranged on the air pipe 35, so as to control the flow of carbon dioxide into the algae The flow rate of the photosynthetic reaction device 3; wherein, the flow controller 23 can be a flow control valve, or any equivalent components.

此外,本发明每一藻类光合反应装置3更可连接一引导管24,其一端设置于透光管路的出口端及加压输液单元32的入口端间,另一端则与上述二氧化碳产生系统100的冷却处理器15的冷凝管路151连通,借以将其冷却蒸汽后所排放的温水引导至此处,以提升培养液的温度,而能利于藻类的生长,尤其是因地区不同或是夜晚而气温较低时,即可利用此方式,从而提升培养液的温度。In addition, each algae photosynthetic reaction device 3 of the present invention can be further connected with a guide pipe 24, one end of which is arranged between the outlet end of the light-transmitting pipeline and the inlet end of the pressurized infusion unit 32, and the other end is connected to the above-mentioned carbon dioxide generation system 100. The condensing pipeline 151 of the cooling processor 15 is connected, so as to guide the warm water discharged after cooling the steam to here, so as to increase the temperature of the culture solution, which can be beneficial to the growth of algae, especially because of different regions or nights. When the temperature is low, this method can be used to increase the temperature of the culture medium.

另,请再搭配图2至图4,本发明的每一藻类光合反应装置3更可进一步包括一连通单元37、一温度调控单元38、一连通管路件39、一洒水单元40及至少一补光单元41。In addition, please match Fig. 2 to Fig. 4 again, each algae photosynthetic reaction device 3 of the present invention can further comprise a communication unit 37, a temperature control unit 38, a communication pipeline member 39, a sprinkler unit 40 and at least one light supplement unit 41 .

连通单元37乃连通于该透光管路的出口端及该加压输液单元32的入口端间,而连通单元37可为一连接管(如图2),或一具开口的储液槽(如图3)皆可。The communication unit 37 is communicated between the outlet end of the light-transmitting pipeline and the inlet end of the pressurized infusion unit 32, and the communication unit 37 can be a connecting pipe (as shown in Figure 2), or a liquid storage tank with an opening ( As shown in Figure 3) can be.

温度调控单元38设置在透光管路的出口端及加压输液单元32的入口端间,而设置在采收阀组件36之前,可设有多个加/降温管381、一入口转接部382及一出口转接部383,该等加/降温管381经由入口转接部382和该出口转接部383可分别连接于该透光管路的出口端和加压输液单元32的入口端之间。温度调控单元38可以手动或自动感应的方式加热容置于该温度调控单元38内的水,使水的热能传递至该等加/降温管381,以控制培养液的温度;或可直接加入冷水于该温度调控单元38内,以降低培养液的温度;或者温度调控单元38可以手动或自动感应的方式直接降低容置于该温度调控单元38内的水,以降低培养液的温度。其中,温度调控单元38可不限于设置在透光管路与加压输液单元32之间处,也可设在其它适当位置处,视方便或需要而设置,以达到加/降温的目的。然而,上述的引导管24亦可直接连接于温度调控单元38,而将温水导引至加/降温管381内,以控制培养液的温度。The temperature regulation unit 38 is arranged between the outlet end of the light-transmitting pipeline and the inlet end of the pressurized infusion unit 32, and is arranged before the recovery valve assembly 36, and can be provided with a plurality of heating/cooling pipes 381 and an inlet adapter. 382 and an outlet adapter 383, the heating/cooling tubes 381 can be respectively connected to the outlet end of the light-transmitting pipeline and the inlet end of the pressurized infusion unit 32 via the inlet adapter 382 and the outlet adapter 383 between. The temperature control unit 38 can manually or automatically heat the water contained in the temperature control unit 38, so that the heat energy of the water can be transferred to the heating/cooling tubes 381 to control the temperature of the culture solution; or can directly add cold water in the temperature control unit 38 to reduce the temperature of the culture solution; or the temperature control unit 38 can directly reduce the water contained in the temperature control unit 38 by manual or automatic induction to reduce the temperature of the culture solution. Wherein, the temperature control unit 38 is not limited to be set between the light-transmitting pipeline and the pressurized infusion unit 32, but also can be set at other appropriate positions, depending on convenience or needs, to achieve the purpose of heating/cooling. However, the above-mentioned guide pipe 24 can also be directly connected to the temperature control unit 38 to guide warm water into the heating/cooling pipe 381 to control the temperature of the culture solution.

连通管路件39连通于该集液筒332底部的出口端及该连通管体34的入口端,该连通管路件39并具有一开关阀组件391,可用以清除较重的沉积物,亦可采样测试该培养液,或者亦可作为采收口。The communication pipeline part 39 communicates with the outlet end of the bottom of the liquid collection tube 332 and the inlet end of the communication pipe body 34. The communication pipeline part 39 also has a switch valve assembly 391, which can be used to remove heavier deposits and also The culture fluid can be sampled and tested, or it can also be used as a collection port.

洒水单元40位于透光管路的上方,并可依环境的需求而以手动或自动感应的方式进行定时定温的洒水,以降低透光管路内的培养液温度。The sprinkler unit 40 is located above the light-transmitting pipeline, and can perform manual or automatic sensory water sprinkling at a fixed time and temperature according to the needs of the environment, so as to reduce the temperature of the culture solution in the light-transmitting pipeline.

如图4所示,补光单元41可为日光灯或其它的光源如LED等,其数量可依实际需求而设置,且同时可设置于透光管路的任一方,如上方或下方等,于本发明的附图中,以位于透光管路的下方为实施例,而补光单元41的光源可适度选为白光、红光或蓝光等,借由补光单元41以提供透光管路可适度调整光度或光源,进而可根据不同藻类所适合的生长环境来改变光源或光度,可用以增加产量以降低成本。As shown in Figure 4, the supplementary light unit 41 can be a fluorescent lamp or other light sources such as LEDs, and its number can be set according to actual needs, and can be set on any side of the light-transmitting pipeline, such as above or below, etc. In the drawings of the present invention, the example is located below the light-transmitting pipeline, and the light source of the supplementary light unit 41 can be appropriately selected as white light, red light, or blue light, etc., and the light-supplementing unit 41 is used to provide a light-transmitting pipeline The luminosity or light source can be adjusted moderately, and then the light source or luminosity can be changed according to the suitable growth environment of different algae, which can be used to increase the output and reduce the cost.

请参阅图5,在本实施例中,连通管体34为一直管,其一端同样地与该光合反应单元31连通,而另一端也是以连通管路件39而连通于集液筒332,而培养液同样经由为直管的连通管体34流入透光管部内以进行循环培养。Please refer to Fig. 5, in the present embodiment, the connecting pipe body 34 is a straight pipe, one end of which is also communicated with the photosynthetic reaction unit 31, and the other end is also communicated with the liquid collection tube 332 through a communication pipe member 39, and The culture solution also flows into the light-transmitting tube part through the connecting tube body 34 which is a straight tube for circulating culture.

由上述,由于该连通管体34的技术效果之一,其使培养液中的藻类微生物于连通管体内具有进行生理调节的目的,但对于生理调节所耗费的时间较短的藻类微生物,则可为一直管以让藻类微生物可以加快流入该透光管路以进行循环培养,而对于需要进行较长时间生理调节的藻类微生物,则需要使用前述为扩张管的连通管体34,以减缓培养液在连通管体34的流速,使得藻类微生物有足够的生理调节的时间。From the above, due to one of the technical effects of the connecting pipe body 34, it enables the algae microorganisms in the culture solution to have the purpose of physiological adjustment in the connecting pipe body, but for the algae microorganisms that take a short time for physiological adjustment, they can It is a straight pipe so that algae microorganisms can speed up the flow into the light-transmitting pipeline for cyclic culture, and for algae microorganisms that need to perform physiological adjustment for a long time, it is necessary to use the aforementioned connecting pipe body 34 that is an expansion pipe to slow down the growth of the culture medium. The flow rate in the connecting pipe body 34 allows the algae microorganisms to have enough time for physiological adjustment.

请再搭配参阅图6,在本发明的每一藻类光合反应装置3可再作不同变化,本实施例中,为了针对不须进行生理调节的特定藻种以加速循环培养,因此,可直接将喷射排氧单元33的集液筒332朝向排氧筒331而将下段向上缩短,而连通管体34即可为一横向流管以连通集液筒332及透光管路,借以使培养液不需进行生理调节的作用,而快速流入透光管路内。Please refer to Fig. 6 again. Different changes can be made in each algae photosynthetic reaction device 3 of the present invention. The liquid collecting cylinder 332 of the spray oxygen exhausting unit 33 faces the oxygen exhausting cylinder 331 and shortens the lower section upwards, and the connecting pipe body 34 can be a horizontal flow pipe to communicate with the liquid collecting cylinder 332 and the light-transmitting pipeline, so that the culture medium does not Need to carry out the function of physiological adjustment, and quickly flow into the light-transmitting pipeline.

请参阅图7,并请配合参阅图2所示;本实施例中,自排氧筒331流落至集液筒332内的培养液,因有些特定的藻种将会黏贴于集液筒332的下段内的壁面上(参阅图2),此乃因藻类的培养液循环至此处时速度减缓,并受压力后会从连通管体34流入至光合反应单元31内,此流速减慢又受压力作用使得特定藻种黏贴于壁面上,亦即就如河川水流减慢时而有沉积污泥的情形,故如图7所示,本发明的每一藻类光合反应装置3更可进一步包含一调节筒体42及一接管43,该调节筒体42底部连通于透光管路的出口端,可连接于上述采收阀组件36的出口端,该接管43连通于调节筒体42的顶部及加压输液单元32的入口端。Please refer to Fig. 7, and refer to Fig. 2 together; in this embodiment, the culture solution flowing from the oxygen exhaust cylinder 331 to the liquid collection cylinder 332 will stick to the liquid collection cylinder 332 because of some specific algae species (referring to Fig. 2), this is because the velocity slows down when the nutrient solution of algae is circulated here, and can flow in the photosynthetic reaction unit 31 from the connecting pipe body 34 after being pressurized, and this flow velocity slows down and is subjected to again. The effect of pressure makes specific algae species stick to the wall surface, that is to say, when the river flow slows down, sludge is deposited. Therefore, as shown in Figure 7, each algae photosynthetic reaction device 3 of the present invention can further include a Regulating cylinder 42 and a connecting pipe 43, the bottom of the regulating cylinder 42 communicates with the outlet end of the light-transmitting pipeline, which can be connected to the outlet end of the above-mentioned recovery valve assembly 36, and the connecting pipe 43 communicates with the top of the regulating cylinder 42 and The inlet port of the pressurized infusion unit 32 .

由上述,当培养液流入调节筒体42内,而液面上升至最顶部后,即可开启该加压输液单元32借由其吸力将培养液强迫流入至喷射排氧单元33内,且集液筒332进一步向上缩短,因此,培养液虽流入至调节筒体42时速度减缓,但受到加压输液单元32的吸力令沉积于壁面上的可能性较少,且流入至集液筒332后能再快速流入至光合反应单元31,而能增加快速循环生产。但,此实施例的缺点,为须增加一些组件(如调节筒体42、接管43或/及接头等)及空间,故制造成本上有增加的情形产生,但若因改变设计后而改善特定藻种沉积黏壁(此沉积表示静止不繁殖)的情形,而能增加快速生产的目的,从而增加产能,即能突破制造成本的缺陷。From the above, when the culture solution flows into the regulating cylinder 42 and the liquid level rises to the top, the pressurized infusion unit 32 can be opened to force the culture solution into the jet oxygen exhaust unit 33 by its suction force, and the collected The liquid cylinder 332 is further shortened upwards. Therefore, although the speed of the culture fluid flowing into the regulating cylinder 42 slows down, it is less likely to be deposited on the wall by the suction force of the pressurized infusion unit 32 , and after flowing into the liquid collection cylinder 332 Can quickly flow into the photosynthetic reaction unit 31 again, and can increase the rapid cycle production. However, the disadvantage of this embodiment is that some components (such as adjusting cylinder 42, connecting pipe 43 or/and joints, etc.) and space must be added, so the manufacturing cost will increase. The situation of algae depositing sticky walls (this deposit means not reproducing), can increase the purpose of rapid production, thereby increasing production capacity, that is, it can break through the defect of manufacturing cost.

另,再如图8所示,为了增加藻类的量产,故可将透光管路的体积增大,当透光管路的长度d为20~30m时,因体积增大而有影响排氧液的排气效果,故为了增加于透光管路的培养液的排气效果,以避免排气效果变差,因而本发明的藻类光合反应装置3可更包括至少一排气单元44,其包含一排气集液筒441、一第一通管442及一第二通管443,第一通管442的入口端连通至透光管路的中段处及出口端连通于排气集液筒441的顶部,第二通管443的入口端连通于排气集液筒441的底部及出口端再连通于透光管路的中段处,而排气集液筒441的顶部末端为开放状。其中,排气集液筒441可设计与上述的排氧筒331和集液筒332相同。In addition, as shown in Figure 8, in order to increase the mass production of algae, the volume of the light-transmitting pipeline can be increased. When the length d of the light-transmitting pipeline is 20-30m, the volume increase will affect the drainage. The exhaust effect of the oxygen liquid, so in order to increase the exhaust effect of the culture solution in the light-transmitting pipeline, so as to avoid the deterioration of the exhaust effect, the algae photosynthetic reaction device 3 of the present invention can further include at least one exhaust unit 44, It includes an exhaust liquid collection cylinder 441, a first through pipe 442 and a second through pipe 443, the inlet end of the first through pipe 442 is connected to the middle section of the light-transmitting pipeline and the outlet end is connected to the exhaust liquid collection The top of the cylinder 441, the inlet end of the second through pipe 443 is connected to the bottom of the exhaust liquid collection cylinder 441 and the outlet end is connected to the middle section of the light-transmitting pipeline, and the top end of the exhaust liquid collection cylinder 441 is open . Wherein, the exhaust liquid collection cylinder 441 can be designed to be the same as the above-mentioned oxygen exhaust cylinder 331 and liquid collection cylinder 332 .

由上述,借以使得再流入至透光管路内的培养液能经由第一通管442流入至排气集液筒441内,而在此处更进一步再次地排放出氧气,培养液可由第二通管443流回至透光管路内。然,排气单元44的数量可依实际需求而设,意即随着透光管路的体积变化及排气等的需求,而可设有二、三或四个以上不等的数量,可作为第二、三、四次等的排气设计。From the above, in order to make the culture solution flowing into the light-transmitting pipeline flow into the exhaust liquid collection tube 441 through the first through pipe 442, and further discharge oxygen again here, the culture solution can be released by the second The through pipe 443 flows back into the light-transmitting pipeline. However, the number of exhaust units 44 can be set according to actual needs, that is, with the volume change of the light-transmitting pipeline and the needs of exhaust, etc., there can be two, three or four or more different quantities, which can be used. As a second, third, fourth, etc. exhaust design.

经由上述的说明,本发明借由藻类生产设备200与二氧化碳产生系统100相结合,借以可将排放出二氧化碳收集再利用,以达到节省排出的目的,同时所生产出的藻类(如蓝藻、红球藻等)具有经济价值而可制成食用品等,或生产出的藻类(如油藻)可提炼出生质油品等。另,每一藻类光合反应装置3借由透光管路、加压输液单元32、喷射排氧单元33及连通管体34的连接组成,使注入于其内的培养液能够呈垂直立体多排管道密封循环地进行光合作用和排氧及吸收二氧化碳,因此,所需占地面积减小、能源使用减少、运转不受天候的影响,可在如半密闭等空间中培养,能避免受污染以维护所产生藻类的质量,尤其是火力发电厂产生的而飘散于大气中的尘埃等。Through the above description, the present invention combines the algae production equipment 200 with the carbon dioxide generation system 100, so that the emitted carbon dioxide can be collected and reused to achieve the purpose of saving discharge, and the produced algae (such as cyanobacteria, red balls Algae, etc.) have economic value and can be made into edible products, etc., or the produced algae (such as oil algae) can be extracted into quality oil products, etc. In addition, each algae photosynthetic reaction device 3 is composed of a light-transmitting pipeline, a pressurized infusion unit 32, a jet oxygen exhaust unit 33 and a connecting pipe body 34, so that the culture solution injected into it can be formed in vertical three-dimensional rows. The pipeline is sealed and cycled for photosynthesis, oxygen exhaust and carbon dioxide absorption. Therefore, the required floor area is reduced, the energy consumption is reduced, and the operation is not affected by the weather. It can be cultivated in a semi-closed space, avoiding pollution and Maintain the quality of the algae produced, especially the dust produced by thermal power plants and scattered in the atmosphere.

因此,请参阅图9,及配合参阅如图2至图7等的附图所示,本发明更提出一种利用光合反应装置以减少二氧化碳的方法,其应用上述说明的系统,该方法如下列所述:Therefore, please refer to Fig. 9, and refer to Fig. 2 to Fig. 7 and other accompanying drawings, the present invention further proposes a method for reducing carbon dioxide by using a photosynthetic reaction device, which uses the system described above, and the method is as follows Said:

(S100)可将水引入二氧化碳产生系统100的锅炉11内,且经燃料(如石油、煤炭或LNG等)燃烧后而产生有蒸汽与二氧化碳。(S100) Water can be introduced into the boiler 11 of the carbon dioxide generation system 100, and the steam and carbon dioxide will be generated after burning fuel (such as petroleum, coal or LNG, etc.).

(S200)上述的蒸汽可引入汽水分离器17后而再引入至加热处理器12,使蒸汽转成高温高压。(S200) The above-mentioned steam can be introduced into the steam-water separator 17 and then introduced into the heating processor 12 to convert the steam into high temperature and high pressure.

(S210)成为高温高压的蒸汽可引入至涡轮机13,以驱动涡轮机13转动使发电机14发电,前述的蒸汽通过冷却处理器15凝结成热水而流入至回流管16。(S210) The high-temperature and high-pressure steam can be introduced into the turbine 13 to drive the turbine 13 to rotate to generate electricity for the generator 14. The aforementioned steam is condensed into hot water through the cooling processor 15 and flows into the return pipe 16.

(S300)上述的二氧化碳引入至藻类生产设备200的涤气处理器21,以净化二氧化碳而去除其含有的有害磷、硫等元素。(S300) The above-mentioned carbon dioxide is introduced into the scrubber 21 of the algae production equipment 200 to purify the carbon dioxide and remove harmful elements such as phosphorus and sulfur contained therein.

(S400)藻类光合反应装置3的透光管路内分别注入有藻类及微生物的培养液,培养液流动于透光管路内以进行光合作用且生成氧气,培养液并流向加压输液单元32。(S400) The light-transmitting pipeline of the algae photosynthetic reaction device 3 is respectively injected with culture fluid of algae and microorganisms, the culture fluid flows in the light-transmitting pipeline to perform photosynthesis and generate oxygen, and the culture fluid flows to the pressurized infusion unit 32 .

(S410)上述的加压输液单元32强迫培养液由输液管321进入至喷射排氧单元33,使培养液冲击于排氧筒331内,以形成一旋转水花状自排氧筒331的上排气口3312排出氧气,培养液落下而收集于集液筒332内。(S410) The above-mentioned pressurized infusion unit 32 forces the culture solution to enter the spray oxygen discharge unit 33 from the infusion tube 321, so that the culture solution impacts in the oxygen discharge cylinder 331 to form a rotating spray-shaped discharge from the top of the oxygen discharge cylinder 331. The air port 3312 exhausts oxygen, and the culture solution falls and is collected in the liquid collection tube 332 .

(S420)上述的二氧化碳由输气管35导入于集液筒332内的培养液中,使培养液的藻类吸收二氧化碳。(S420) The above-mentioned carbon dioxide is introduced into the culture solution in the liquid collection tank 332 through the gas delivery pipe 35, so that the algae in the culture solution absorb carbon dioxide.

(S430)上述的培养液由连通管体34再流入至透光管路内,以再次进行光合作用而再生成氧气。(S430) The above-mentioned culture solution flows into the light-transmitting pipeline through the connecting pipe body 34, so as to perform photosynthesis again and generate oxygen again.

另,上述的每一藻类光合反应装置3更提供一采收阀组件36,再次光合作用后的培养液流经透光管路后,由采收阀组件36汲取该再次光合作用后的培养液。In addition, each of the above-mentioned algae photosynthetic reaction devices 3 further provides a harvesting valve assembly 36, after the culture fluid after photosynthesis flows through the light-transmitting pipeline again, the culture fluid after the photosynthesis is drawn by the harvesting valve assembly 36 .

另,上述的培养液皆以循序环流的方式由上而下流动于该透光管路内。In addition, the above-mentioned culture solution flows in the light-transmitting pipeline from top to bottom in a sequential circulation manner.

另,上述的每一藻类光合反应装置3更可提供一温度调控单元38,培养液流经温度调控单元38后,再流向加压输液单元32,以控制调升/降培养液的温度。In addition, each algae photosynthetic reaction device 3 mentioned above can further provide a temperature control unit 38, after the culture solution flows through the temperature control unit 38, then flows to the pressurized infusion unit 32 to control the temperature of the culture solution.

另,上述的每一藻类光合反应装置3更提供一洒水单元40,当培养液流于透光管路,该洒水单元40可依工作环境的需求而洒水于该透光管路上,以降低该透光管路内的培养液的温度。In addition, each of the above-mentioned algae photosynthetic reaction devices 3 further provides a sprinkler unit 40. When the culture solution flows in the light-transmitting pipeline, the water-sprinkling unit 40 can sprinkle water on the light-transmitting pipeline according to the needs of the working environment, so as to reduce the The temperature of the culture solution in the light-transmitting pipeline.

另,上述的藻类生产设备200更可提供一温变调控器22,二氧化碳经涤气处理器21后,更导入于温变调控器22使二氧化碳的温度降温,再导入于该等藻类光合反应装置3,借以将二氧化碳调控至适当的温度,可避免温度过高使培养液的藻类死亡。In addition, the above-mentioned algae production equipment 200 can further provide a temperature change controller 22. After the carbon dioxide passes through the scrubber 21, it is further introduced into the temperature change controller 22 to lower the temperature of the carbon dioxide, and then introduced into the algae photosynthetic reaction devices. 3. By adjusting the carbon dioxide to an appropriate temperature, the algae in the culture solution can be prevented from dying due to excessive temperature.

另,上述的藻类生产设备200更可提供一流量控制器23,二氧化碳经涤气处理器21后,更导入于流量控制器23以控制该二氧化碳流入于该等藻类光合反应装置3的集液筒332内的流量。In addition, the above-mentioned algae production equipment 200 can further provide a flow controller 23, after the carbon dioxide passes through the scrubber 21, it is further introduced into the flow controller 23 to control the flow of the carbon dioxide into the liquid collection cylinder of the algae photosynthetic reaction device 3 332 traffic.

另,上述的每一藻类光合反应装置3更提供至少一补光单元41,其照射该透光管路,用以可适度调整该透光管路内的培养液所需的光度或光源。In addition, each algae photosynthetic reaction device 3 mentioned above further provides at least one supplementary light unit 41, which illuminates the light-transmitting pipeline, so as to properly adjust the luminosity or light source required by the culture solution in the light-transmitting pipeline.

综合上述的说明,通过本发明利用光合反应装置以减少二氧化碳的系统及方法,具有如下的特点:Based on the above description, the system and method for reducing carbon dioxide by using the photosynthetic reaction device of the present invention have the following characteristics:

1、借由藻类生产设备200与二氧化碳产生系统100相结合,借以可将排放出二氧化碳收集再利用,以达到减少二氧化碳排出于大气中的目的。1. By combining the algae production equipment 200 with the carbon dioxide generation system 100, the discharged carbon dioxide can be collected and reused, so as to reduce the discharge of carbon dioxide into the atmosphere.

2、藻类生产设备200的每一藻类光合反应装置3所生产出的藻类具有经济价值而可制成食用品、保健品或提炼出油品等。2. The algae produced by each algae photosynthetic reaction device 3 of the algae production equipment 200 has economic value and can be made into food products, health products or refined oil products.

3、每一藻类光合反应装置3借由透光管路、加压输液单元32、喷射排氧单元33及连通管体34的连接组成,使注入于其内的培养液能够呈垂直立体多排管道密封循环地进行光合作用和排氧及吸收二氧化碳,具有所需占地面积小、能源使用减少、运转不受天候的影响等效用,能避免受污染以维护所产生藻类的质量,故可大量化摆设于发力发电厂适当的场所处。3. Each algae photosynthetic reaction device 3 is composed of a light-transmitting pipeline, a pressurized infusion unit 32, a jet oxygen exhaust unit 33 and a connecting pipe body 34, so that the culture solution injected into it can be vertically arranged in multiple rows. The pipeline is sealed and cycled for photosynthesis, oxygen exhaust and carbon dioxide absorption. It has the advantages of small footprint, reduced energy consumption, and operation not affected by the weather. It can avoid pollution to maintain the quality of the produced algae, so it can be used in large quantities. The chemical display is placed at the appropriate place of the power plant.

4、每一藻类光合反应装置3的排氧筒331和集液筒332的组接,及透光管路的设计,使得每一藻类光合反应装置3易于清洗、维护,以确保光合作用的效果和藻类的质量。4. The assembly of the oxygen exhaust cylinder 331 and the liquid collection cylinder 332 of each algae photosynthetic reaction device 3, and the design of the light-transmitting pipeline make each algae photosynthetic reaction device 3 easy to clean and maintain, so as to ensure the effect of photosynthesis and algae quality.

5、引导管24、温度调控单元38、洒水单元40和补光单元41的配置,可依地域、季节、天候的不同或依培养液的需求而设置,进而可作适当的温度调节,使其能有效地控制培养液的温度,及可适度调整光度或光源。5. The configuration of the guide pipe 24, the temperature control unit 38, the sprinkler unit 40 and the supplementary light unit 41 can be set according to different regions, seasons, weather or according to the needs of the culture medium, and then can be properly adjusted to make it It can effectively control the temperature of the culture medium, and can moderately adjust the luminosity or light source.

但是,上述所揭示的附图、说明,仅为本发明的实施例而已,凡本领域的普通技术人员可依据上述的说明作其它种种的改进,而这些改变仍属于本发明的发明精神及界定的权利要求范围中。However, the drawings and descriptions disclosed above are only embodiments of the present invention, and those skilled in the art can make other various improvements based on the above descriptions, and these changes still belong to the spirit and definition of the present invention. within the scope of the claims.

Claims (21)

1.一种利用光合反应装置以减少二氧化碳的系统,其特征在于,包括:1. A system utilizing a photosynthetic reaction device to reduce carbon dioxide, characterized in that it comprises: 一二氧化碳产生系统,其包含有一产生二氧化碳的锅炉;以及a carbon dioxide generating system comprising a boiler for generating carbon dioxide; and 一藻类生产设备,其包含一与该锅炉连通的涤气处理器及多个与该涤气处理器连通的藻类光合反应装置,每一藻类光合反应装置包括:An algae production equipment comprising a scrubber connected to the boiler and a plurality of algae photosynthetic reaction units connected to the scrubber, each algae photosynthetic unit comprising: 一光合反应单元,其为透光管路;A photosynthetic reaction unit, which is a light-transmitting pipeline; 一加压输液单元,其与该透光管路连通,该加压输液单元具有一输液管;A pressurized infusion unit, which communicates with the light-transmitting pipeline, and the pressurized infusion unit has an infusion tube; 一喷射排氧单元,其为中空筒件而具有相组接的一排氧筒与一集液筒,该排氧筒设有一进液口、一上排气口和一中空管壁,该进液口连通于该输液管的出口端,该上排气口位于该排氧筒的顶端,该中空管壁自该上排气口向下延伸;A spray oxygen exhaust unit, which is a hollow cylinder and has an oxygen exhaust cylinder and a liquid collection cylinder assembled together. The oxygen exhaust cylinder is provided with a liquid inlet, an upper exhaust port and a hollow pipe wall. The inlet The liquid port is connected to the outlet end of the infusion tube, the upper exhaust port is located at the top of the oxygen exhaust cylinder, and the hollow pipe wall extends downward from the upper exhaust port; 一连通管体,其连通该集液筒及该透光管路;及a connecting pipe body, which connects the liquid collection tube and the light-transmitting pipeline; and 一输气管,其一端与该涤气处理器连通,另一端伸入至该集液筒内。A gas delivery pipe, one end of which communicates with the scrubber, and the other end extends into the liquid collection cylinder. 2.如权利要求1所述的利用光合反应装置以减少二氧化碳的系统,其特征在于,该二氧化碳产生系统更包含一与该锅炉连通的汽水分离器、一与该汽水分离器连通的加热处理器、一与该加热处理器连通的涡轮机、一与该涡轮机连结的发电机、一与该涡轮机连通的冷却处理器及一与该冷却处理器连通的回流管。2. The system for reducing carbon dioxide utilizing a photosynthetic reaction device as claimed in claim 1, wherein the carbon dioxide generating system further comprises a steam separator communicated with the boiler, a heating processor communicated with the steam separator , a turbine in communication with the heating processor, a generator in communication with the turbine, a cooling processor in communication with the turbine, and a return pipe in communication with the cooling processor. 3.如权利要求2所述的利用光合反应装置以减少二氧化碳的系统,其特征在于,每一藻类光合反应装置更连接一引导管,该引导管一端设置于该透光管路的出口端及该加压输液单元的入口端之间,另一端与该二氧化碳产生系统的冷却处理具有的冷凝管路连通。3. The system for reducing carbon dioxide by using a photosynthetic reaction device as claimed in claim 2, wherein each algae photosynthetic reaction device is further connected with a guide tube, and one end of the guide tube is arranged at the outlet end of the light-transmitting pipeline and Between the inlet ends of the pressurized infusion unit, the other end communicates with the condensation pipeline of the cooling process of the carbon dioxide generating system. 4.如权利要求1所述的利用光合反应装置以减少二氧化碳的系统,其特征在于,每一藻类光合反应装置的光合反应单元包括多个直管和多个弯管,该等直管和该等弯管间隔串接形成一双排倾斜的立体盘旋式透光管路。4. Utilize photosynthetic reaction device as claimed in claim 1 to reduce the system of carbon dioxide, it is characterized in that, the photosynthetic reaction unit of each algae photosynthetic reaction device comprises a plurality of straight pipes and a plurality of curved pipes, and these straight pipes and the Equal curved tubes are connected in series at intervals to form a double-row inclined three-dimensional spiral light-transmitting pipeline. 5.如权利要求所述的利用光合反应装置以减少二氧化碳的系统,其特征在于,每一藻类光合反应装置的排氧筒的中段设有一缩颈部和一侧排气口,该侧排气口位于该缩颈部的下方。5. Utilize the photosynthetic reaction device as claimed in claim to reduce the system of carbon dioxide, it is characterized in that, the middle section of the oxygen exhaust cylinder of each algae photosynthetic reaction device is provided with a constriction and a side exhaust port, and the side exhaust The mouth is located below the constriction. 6.如权利要求5所述的利用光合反应装置以减少二氧化碳的系统,其特征在于,每一藻类光合反应装置的喷射排氧单元更包括一排气管,该排气管组接于该排氧筒内,该排气管的上端穿设于该中空管壁内,该排气管的下端进一步形成一扩张部且相对地位于该侧排气口的内侧。6. The system for reducing carbon dioxide by using a photosynthetic reaction device as claimed in claim 5, wherein the jet oxygen exhaust unit of each algae photosynthetic reaction device further includes an exhaust pipe, and the exhaust pipe is connected to the exhaust pipe. In the oxygen cylinder, the upper end of the exhaust pipe is pierced in the hollow tube wall, and the lower end of the exhaust pipe further forms an expansion part and is relatively located inside the side exhaust port. 7.如权利要求1所述的利用光合反应装置以减少二氧化碳的系统,其特征在于,每一藻类光合反应装置更包括一采收阀组件,该采收阀组件连通于该透光管路的出口端与该加压输液单元的入口端之间。7. The system for reducing carbon dioxide by using a photosynthetic reaction device as claimed in claim 1, wherein each algae photosynthetic reaction device further comprises a recovery valve assembly, which is connected to the transparent pipeline. between the outlet port and the inlet port of the pressurized infusion unit. 8.如权利要求1所述的利用光合反应装置以减少二氧化碳的系统,其特征在于,每一藻类光合反应装置更包括一温度调控单元,该温度调控单元设置在该透光管路的出口端及该加压输液单元的入口端之间。8. The system for reducing carbon dioxide by utilizing a photosynthetic reaction device as claimed in claim 1, wherein each algae photosynthetic reaction device further comprises a temperature control unit, and the temperature control unit is arranged at the outlet end of the light-transmitting pipeline and the inlet port of the pressurized infusion unit. 9.如权利要求1所述的利用光合反应装置以减少二氧化碳的系统,其特征在于,每一藻类光合反应装置更包括:9. The system for reducing carbon dioxide by utilizing a photosynthetic reaction device as claimed in claim 1, wherein each algae photosynthetic reaction device further comprises: 一连通单元,其连通于该透光管路的出口端及该加压输液单元的入口端之间;A communication unit, which communicates between the outlet end of the light-transmitting pipeline and the inlet end of the pressurized infusion unit; 一连通管路件,其连通于该集液筒底部的出口端及该连通管体的入口端,该连通管路件并具有一开关阀组件;A communication pipeline member, which communicates with the outlet end of the bottom of the liquid collection tube and the inlet end of the communication pipe body, and the communication pipeline member also has a switch valve assembly; 一洒水单元,其位于该透光管路的上方;及a sprinkler unit located above the light-transmitting pipeline; and 至少一补光单元,其位于该透光管路的一方。At least one supplementary light unit is located on one side of the light-transmitting pipeline. 10.如权利要求1所述的利用光合反应装置以减少二氧化碳的系统,其特征在于,每一藻类光合反应装置更包括一调节筒体及一接管,该调节筒体的底部连通于该透光管路的出口端,该接管连通该调节筒体的顶端及该加压输液单元的入口端。10. The system for reducing carbon dioxide by using a photosynthetic reaction device as claimed in claim 1, wherein each algae photosynthetic reaction device further includes a regulating cylinder and a connecting pipe, and the bottom of the regulating cylinder communicates with the light-transmitting The outlet end of the pipeline, the connecting pipe communicates with the top end of the regulating cylinder and the inlet end of the pressurized infusion unit. 11.如权利要求1所述的利用光合反应装置以减少二氧化碳的系统,其特征在于,每一藻类光合反应装置更包括至少一排气单元,该排气单元包含一排气集液筒、一第一通管及一第二通管,该第一通管的入口端连通于该透光管路及出口端连通于该排气管的顶部,该第二通管的入口端连通于该排气筒的底部及出口端连通于透光管路。11. The system for reducing carbon dioxide by using a photosynthetic reaction device as claimed in claim 1, wherein each algae photosynthetic reaction device further comprises at least one exhaust unit, and the exhaust unit comprises an exhaust liquid collection cylinder, an A first through pipe and a second through pipe, the inlet end of the first through pipe communicates with the light-transmitting pipeline and the outlet end communicates with the top of the exhaust pipe, the inlet end of the second through pipe communicates with the row The bottom and the outlet end of the gas cylinder are communicated with the light-transmitting pipeline. 12.如权利要求1所述的利用光合反应装置以减少二氧化碳的系统,其特征在于,该藻类生产设备更包括一流量控制器,该流量控制器连结于该涤气处理器及该等藻类光合反应装置之间,该等藻类光合反应装置的输气管与该流量控制器连通。12. The system for reducing carbon dioxide by using a photosynthetic reaction device as claimed in claim 1, wherein the algae production equipment further comprises a flow controller connected to the scrubber and the photosynthetic algae Between the reaction devices, the air pipes of the algae photosynthetic reaction devices communicate with the flow controller. 13.如权利要求1所述的利用光合反应装置以减少二氧化碳的系统,其特征在于,该藻类生产设备更包括一温变调控器,该温变调控器连通于该涤气处理器之后与该等藻类光合反应装置间。13. The system for reducing carbon dioxide by using a photosynthetic reaction device as claimed in claim 1, wherein the algae production equipment further comprises a temperature change regulator, and the temperature change regulator is communicated with the scrubber after the gas scrubber and other algal photosynthetic reaction devices. 14.一种利用光合反应装置以减少二氧化碳的方法,其特征在于,利用权利要求1所述的利用光合反应装置以减少二氧化碳的系统,该方法包括:14. A method of utilizing a photosynthetic reaction device to reduce carbon dioxide, characterized in that, utilizing the system of utilizing a photosynthetic reaction device according to claim 1 to reduce carbon dioxide, the method comprises: 该二氧化碳产生系统的锅炉经燃料燃烧后产生有二氧化碳;The boiler of the carbon dioxide generating system produces carbon dioxide after fuel combustion; 上述的二氧化碳引入至该藻类生产设备的涤气处理器,以净化该二氧化碳;The above-mentioned carbon dioxide is introduced into the scrubber of the algae production equipment to purify the carbon dioxide; 该等藻类光合反应装置的透光管路内分别注入有藻类及微生物的培养液,该培养液流动于该透光管路内以进行光合作用且生成氧气,该培养液并流向该加压输液单元;The light-transmitting pipelines of these algae photosynthetic reaction devices are respectively injected with culture fluids of algae and microorganisms, and the culture fluid flows in the light-transmitting pipelines to perform photosynthesis and generate oxygen, and the culture fluid flows to the pressurized infusion fluid unit; 上述的加压输液单元强迫该培养液由该输液管进入至该喷射排氧单元,使该培养液冲击于该排氧筒内,以形成一旋转水花扩散飞溅状自该上排气口排出氧气,该培养液落下收集于该集液筒;The above-mentioned pressurized infusion unit forces the culture solution to enter the spray oxygen exhaust unit from the infusion tube, so that the culture solution impacts in the oxygen exhaust cylinder to form a rotating water splash to discharge oxygen from the upper exhaust port. , the culture solution falls and is collected in the collection tube; 上述的二氧化碳由该输气管导入于该集液筒内的培养液中,使该培养液的藻类吸收该二氧化碳;以及The above-mentioned carbon dioxide is introduced into the culture solution in the liquid collection tube through the gas delivery pipe, so that the algae in the culture solution can absorb the carbon dioxide; and 上述的培养液由该连通管体再流入至该透光管路内,以再次进行光合作用而生成氧气。The above-mentioned culture solution flows into the light-transmitting pipeline through the connecting pipe body, so as to perform photosynthesis again to generate oxygen. 15.如权利要求14所述的利用光合反应装置以减少二氧化碳的方法,其特征在于,每一藻类光合反应装置更提供一采收阀组件,再次光合作用后的培养液流经该透光管路后,由该采收阀组件汲取该再次光合作用后的培养液。15. The method of utilizing a photosynthetic reaction device to reduce carbon dioxide as claimed in claim 14, wherein each algae photosynthetic reaction device further provides a harvesting valve assembly, and the culture solution after photosynthesis again flows through the light-transmitting tube After the passage, the re-photosynthesized culture fluid is drawn by the recovery valve assembly. 16.如权利要求14所述的利用光合反应装置以减少二氧化碳的方法,其特征在于,所述的培养液皆以循序环流的方式由上而下流动于该透光管路内。16 . The method for reducing carbon dioxide by using a photosynthetic reaction device as claimed in claim 14 , wherein the culture solution flows through the light-transmitting pipeline from top to bottom in a sequential circulation manner. 17 . 17.如权利要求14所述的利用光合反应装置以减少二氧化碳的方法,其特征在于,每一藻类光合反应装置更提供一温度调控单元,该培养液流经该温度调控单元后,再流向该加压输液单元。17. The method for reducing carbon dioxide by using a photosynthetic reaction device as claimed in claim 14, wherein each algae photosynthetic reaction device further provides a temperature control unit, and after the culture fluid flows through the temperature control unit, it flows to the Pressurized infusion unit. 18.如权利要求14所述的利用光合反应装置以减少二氧化碳的方法,其特征在于,每一藻类光合反应装置更提供一洒水单元,当该培养液流于该透光管路时,该洒水单元洒水于该透光管路上。18. The method for reducing carbon dioxide by utilizing a photosynthetic reaction device as claimed in claim 14, wherein each algae photosynthetic reaction device further provides a sprinkler unit, and when the culture fluid flows in the light-transmitting pipeline, the sprinkler unit The unit sprinkles water on the transparent pipe. 19.如权利要求14所述的利用光合反应装置以减少二氧化碳的方法,其特征在于,每一藻类光合反应装置更提供至少一补光单元,该补光单元照射该透光管路。19. The method for reducing carbon dioxide by using a photosynthetic reaction device as claimed in claim 14, wherein each algae photosynthetic reaction device further provides at least one supplementary light unit, and the supplementary light unit illuminates the light-transmitting pipeline. 20.如权利要求14所述的利用光合反应装置以减少二氧化碳的方法,其特征在于,该藻类生产设备更提供一温变调控器,该二氧化碳经该涤气处理器后,更导入于该温变调控器使该二氧化碳的温度降温,再导入于该等藻类光合反应装置。20. The method for reducing carbon dioxide by using a photosynthetic reaction device as claimed in claim 14, wherein the algae production equipment further provides a temperature regulator, and the carbon dioxide is further introduced into the temperature controller after passing through the scrubber. The variable regulator lowers the temperature of the carbon dioxide, and then introduces it into the algae photosynthetic reaction devices. 21.如权利要求14所述的利用光合反应装置以减少二氧化碳的方法,其特征在于,该藻类生产设备更提供一流量控制器,该二氧化碳经该涤气处理器后,更导入于该流量控制器以控制该二氧化碳流入于该等藻类光合反应装置的集液筒内的流量。21. The method for reducing carbon dioxide by using a photosynthetic reaction device as claimed in claim 14, wherein the algae production equipment further provides a flow controller, and the carbon dioxide is further introduced into the flow controller after passing through the scrubber. A device is used to control the flow rate of the carbon dioxide flowing into the liquid collection tubes of the algae photosynthetic reaction devices.
CN200810192993A 2008-12-31 2008-12-31 System and method for reducing carbon dioxide using photosynthetic reaction device Pending CN101766955A (en)

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Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN103301746A (en) * 2012-03-16 2013-09-18 赖珏光 Method and system for sequestering carbon dioxide in combination with shellfish or coral farming
CN105797572A (en) * 2016-03-23 2016-07-27 凯天环保科技股份有限公司 Reaction bed for purifying CO2 through biological method
CN105854581A (en) * 2016-03-23 2016-08-17 凯天环保科技股份有限公司 CO2 purifier

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN103301746A (en) * 2012-03-16 2013-09-18 赖珏光 Method and system for sequestering carbon dioxide in combination with shellfish or coral farming
CN105797572A (en) * 2016-03-23 2016-07-27 凯天环保科技股份有限公司 Reaction bed for purifying CO2 through biological method
CN105854581A (en) * 2016-03-23 2016-08-17 凯天环保科技股份有限公司 CO2 purifier
CN105854581B (en) * 2016-03-23 2018-09-25 航天凯天环保科技股份有限公司 A kind of CO2Purifier
CN105797572B (en) * 2016-03-23 2018-11-20 航天凯天环保科技股份有限公司 A kind of biological method purification CO2Reaction bed

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