CN101766955A - System and method for reducing carbon dioxide using photosynthetic reaction device - Google Patents
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- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 title claims abstract description 222
- 230000000243 photosynthetic effect Effects 0.000 title claims abstract description 112
- 229910002092 carbon dioxide Inorganic materials 0.000 title claims abstract description 111
- 239000001569 carbon dioxide Substances 0.000 title claims abstract description 111
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- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 claims description 59
- 229910052760 oxygen Inorganic materials 0.000 claims description 59
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- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
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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。
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.
Description
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
锅炉11 加热处理器12Boiler 11
涡轮机13 发电机14Turbine 13
冷却处理器15 冷凝管路151
回流管16 汽水分离器17
藻类生产设备200
涤气处理器21 温变调控器22Scrubbing
流量控制器23 引导管24
藻类光合反应装置3Algae
光合反应单元31
直管311 弯管312
辅助开口313
加压输液单元32Pressurized
输液管321
喷射排氧单元33Jet
排氧筒331
进液口3311 上排气口3312
缩颈部3313 侧排气口3314Neck 3313
集液筒332
中空管壁333
排气管334exhaust
扩张部3341
连通管体34Connecting
输气管35
采收阀组件36
连通单元37
温度调控单元38
加/降温管381 入口转接部382Adding/
出口转接部383
连通管路件39Connecting
开关阀组件391
洒水单元40
补光单元41
调节筒体42Regulating
接管43Take over 43
排气单元44
排气集液筒441 第一通管442Exhaust
第二通管443Second through
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 )
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
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
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
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
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
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
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
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
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
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
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
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
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
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
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
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
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
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
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
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
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
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
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
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
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
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
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
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
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
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
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
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
(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-
(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
(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
(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
(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
(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
(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
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
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
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
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
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
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
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
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
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
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
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
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.
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Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
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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 |
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Cited By (5)
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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