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CN102660451B - Horizontal immersion cover type carbon supplement device and carbon supplement method used in culture of microalgae in open pond - Google Patents

Horizontal immersion cover type carbon supplement device and carbon supplement method used in culture of microalgae in open pond Download PDF

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CN102660451B
CN102660451B CN201210138845.8A CN201210138845A CN102660451B CN 102660451 B CN102660451 B CN 102660451B CN 201210138845 A CN201210138845 A CN 201210138845A CN 102660451 B CN102660451 B CN 102660451B
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丛威
刘明
吴霞
温树梅
张东梅
孙中亮
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Abstract

本发明涉及微藻培养领域,具体地,本发明涉及用于开放池培养微藻的水平浸没罩式补碳装置及其补碳方法。本发明的用于开放池培养微藻的水平浸没罩式补碳装置,包括一个或两个以上罩子(1)和气体分布器(2),所述气体分布器(2)设置于开放池底部,所述罩子(1)罩于气体分布器(2)上方,该罩子(1)呈两端开口的筒体,沿培养液流动方向布置,罩子(1)的两端口分别为培养液进口(3)和培养液出口(4);其中,所述气体分布器(2)与罩子(1)的培养液出口(4)距离40厘米以上。本发明,在开放池内培养微藻细胞时,能够有效利用二氧化碳进行补碳,大大降低了生产成本。

Figure 201210138845

The invention relates to the field of microalgae cultivation, in particular, the invention relates to a horizontal immersion cover type carbon replenishing device and a carbon replenishing method for cultivating microalgae in an open pool. The horizontal immersion hood type carbon replenishment device for cultivating microalgae in an open pool of the present invention includes one or more covers (1) and a gas distributor (2), and the gas distributor (2) is arranged at the bottom of the open pool , the cover (1) is placed above the gas distributor (2), the cover (1) is a cylinder with two ends open, arranged along the flow direction of the culture solution, and the two ports of the cover (1) are the inlets of the culture solution ( 3) and the culture solution outlet (4); wherein, the distance between the gas distributor (2) and the culture solution outlet (4) of the cover (1) is more than 40 cm. In the present invention, when microalgae cells are cultivated in an open pool, carbon dioxide can be effectively used for carbon replenishment, and the production cost is greatly reduced.

Figure 201210138845

Description

用于开放池培养微藻的水平浸没罩式补碳装置及其补碳方法Horizontal immersion cover type carbon replenishment device and carbon replenishment method for cultivating microalgae in open ponds

技术领域 technical field

本发明涉及微藻培养领域,具体地,本发明涉及用于开放池培养微藻的水平浸没罩式补碳装置及其补碳方法。The invention relates to the field of microalgae cultivation, in particular, the invention relates to a horizontal immersion cover type carbon replenishing device and a carbon replenishing method for cultivating microalgae in an open pool.

背景技术 Background technique

微藻可以通过光合作用固定二氧化碳生产多种化学品。有的可以产脂肪烃,如葡萄藻产烃量可达细胞干重的15%~75%,有的可积累糖原,有的可积累甘油,许多微藻含油脂可达干重的60%以上。藻类热解所获得的生物质燃油热值平均高达33MJ/kg。微藻可以在海水、碱水或半碱水中培养,不与农作物争夺土地和淡水资源,还可以利用废水,是淡水短缺、土地贫瘠地区获得有效生物资源的重要途径。微藻有望成为未来的能源和化学品的重要来源。Microalgae can fix carbon dioxide through photosynthesis to produce a variety of chemicals. Some can produce aliphatic hydrocarbons, such as grape algae, which can produce hydrocarbons up to 15% to 75% of dry cell weight, some can accumulate glycogen, and some can accumulate glycerol, and many microalgae contain oil up to 60% of dry weight above. The average calorific value of biomass fuel obtained from algae pyrolysis is as high as 33MJ/kg. Microalgae can be cultivated in seawater, alkaline water or semi-alkaline water, without competing with crops for land and freshwater resources, and can also use wastewater, which is an important way to obtain effective biological resources in areas with freshwater shortages and barren land. Microalgae promise to be an important source of future energy and chemicals.

微藻细胞中碳的含量占其细胞干重的一半以上,藻细胞在生长过程中通过光合作用将二氧化碳固定为自身的组成成分,故在藻类培养过程中需在培养液中保持碳源的供给。藻类培养液中的无机碳源以HCO3 -、CO3 2-和游离的CO2三种形式存在。三种形式的碳在水溶液中的含量比例随pH值的变化而变化。若使用小苏打(NaHCO3)为碳源,则随着HCO3 -的解离和CO2的利用,培养液的pH值逐渐升高,有超过一半的NaHCO3转化为Na2CO3而不能被利用,碳源消耗大,培养液pH升高导致水体难以循环利用。若直接以CO2为碳源,微藻利用的就是CO2,则可以避免培养液pH值升高的问题,有利于维持适宜的培养环境,使水可以长时间或者重复使用。The carbon content in microalgae cells accounts for more than half of its dry weight. During the growth process, algae cells fix carbon dioxide as their own components through photosynthesis. Therefore, it is necessary to maintain the supply of carbon sources in the culture medium during algae cultivation. . Inorganic carbon sources in algae culture fluid exist in three forms: HCO 3 - , CO 3 2- and free CO 2 . The proportions of the three forms of carbon in aqueous solutions vary with pH. If baking soda (NaHCO 3 ) is used as the carbon source, then with the dissociation of HCO 3 - and the utilization of CO 2 , the pH value of the culture solution will gradually increase, and more than half of the NaHCO 3 will be converted into Na 2 CO 3 and cannot If it is used, the consumption of carbon source is large, and the pH of the culture medium increases, which makes it difficult to recycle the water body. If CO 2 is directly used as the carbon source, the microalgae utilizes CO 2 , which can avoid the problem of increasing the pH value of the culture solution, and is conducive to maintaining a suitable culture environment, so that the water can be used for a long time or repeatedly.

开放式培养是传统而又简单的微藻培养模式,也是目前被大家公认为是成熟的微藻培养技术,优点是构建简单、操作简便,在螺旋藻、小球藻和盐藻的工业化生产中获得了应用(Chaumont D.,J.Appl.Phycol.,1993,5:593-604;Richmond A.,Progress in Physiological Research,Vol.7,Biopress,Bristol.,1990,269-330;BorowitzkaL.T.,Bioresource Technology,1991,38:251-252)。然而,传统开放池由于液层深度20~30cm,如果以鼓泡的方式直接向培养池中补加CO2,由于气泡在培养液中停留时间短,使得CO2的吸收率非常低,只有13%~20%的CO2被吸收(Becker EW,Microalgae:biotechnology and microbiology.Cambridge University Press,Cambridge,1994,pp293)。Open culture is a traditional and simple microalgae culture mode, and is currently recognized as a mature microalgae culture technology. The advantages are simple construction and easy operation. It is used in the industrial production of spirulina, chlorella and salina Applied (Chaumont D., J.Appl.Phycol., 1993, 5:593-604; Richmond A., Progress in Physiological Research, Vol.7, Biopress, Bristol., 1990, 269-330; BorowitzkaL.T ., Bioresource Technology, 1991, 38:251-252). However, because the depth of the liquid layer in the traditional open pool is 20-30 cm, if CO 2 is directly added to the culture tank by bubbling, the CO 2 absorption rate is very low, only 13 % to 20% of CO 2 is absorbed (Becker EW, Microalgae: biotechnology and microbiology. Cambridge University Press, Cambridge, 1994, pp293).

Ferreira等(Ferreira B S,Fernandes H L,Reis A and Mateus M.Microporous hollowfibres for carbon dioxide absorption:mass transfer model fitting and the supplying ofcarbon dioxide to microalgae cultures.Journal of Chemical Technology andBiotechnology,1998,71:61-70)利用中空纤维膜来强化气液传质,以提高CO2的吸收率,但该法造价高,中空纤维膜易受污染。Ferreira et al. (Ferreira B S, Fernandes H L, Reis A and Mateus M. Microporous hollow fibers for carbon dioxide absorption: mass transfer model fitting and the supplying of carbon dioxide to microalgae cultures. Journal of Chemical Technology and Biotechnology, 1998, 71: 61-70) used Hollow fiber membranes are used to enhance gas-liquid mass transfer to increase the absorption rate of CO 2 , but this method is expensive and the hollow fiber membranes are easily polluted.

气罩法(李夜光,胡鸿钧,张良军,陈志祥。以二氧化碳为碳源工业化生产螺旋藻工艺技术的研究。武汉植物学研究,1996,14(4):349-356)是在微藻养殖水面上扣一个几平米的罩子,将二氧化碳气体通入罩子内,依靠罩子扣住的水面向培养液传递二氧化碳。该方法的问题在于气液交换的比表面积小;气罩内会积累氧气、氮气从而降低传质速率,需要不断放空,从而损失气罩内的二氧化碳;对于含低浓度二氧化碳的气源,二氧化碳的吸收率很低;而且气罩内压力稍高时气体会从气罩下方穿过气罩外的液面漏出。槽式补碳(CN200610018771.9,微藻养殖池补充二氧化碳的装置)是在培养池边挖一个深槽,使培养液流过深槽,在槽底布置通气管,向培养液供应二氧化碳,该方法会打乱传统的开放池的空间布局,且在槽内缺少混合,一段时间后槽的底部被二氧化碳饱和后就成为传质的死区,失去了深槽的作用。The gas mask method (Li Yeguang, Hu Hongjun, Zhang Liangjun, Chen Zhixiang. Research on the technology of industrial production of spirulina with carbon dioxide as carbon source. Wuhan Botanical Research, 1996,14(4):349-356) is on the water surface of microalgae culture Buckle a cover of a few square meters, pass carbon dioxide gas into the cover, and rely on the water covered by the cover to transfer carbon dioxide to the culture solution. The problem with this method is that the specific surface area of gas-liquid exchange is small; Oxygen and nitrogen will accumulate in the gas hood to reduce the mass transfer rate, and it needs to be continuously vented, thereby losing the carbon dioxide in the gas hood; The absorption rate is very low; and when the pressure in the gas hood is slightly higher, the gas will leak from the bottom of the gas hood through the liquid surface outside the gas hood. Trough carbon replenishment (CN200610018771.9, a device for supplementing carbon dioxide in microalgae culture ponds) is to dig a deep groove at the side of the culture pond, let the culture solution flow through the deep groove, and arrange a ventilation pipe at the bottom of the groove to supply carbon dioxide to the culture solution. This method will disrupt the spatial layout of the traditional open pool, and there is a lack of mixing in the tank. After a period of time, the bottom of the tank is saturated with carbon dioxide and becomes a dead zone for mass transfer, losing the role of a deep tank.

丛威等(CN200510126465.2用于大规模培养微藻的补碳装置及其使用方法和用途)发明了在开放池直接为培养液补充CO2的阱式补碳装置,使培养液在阱式补碳装置内形成环流,大幅度延长了气液接触时间,并从阱式补碳装置的底部供气,大幅度提高了CO2的吸收率。但是此补碳装置增加了开放池内流体的流动阻力,导致在保持同样流速情况下叶轮驱动流体的电能消耗增加,此外施工的工程量偏大。Cong Wei et al. (CN200510126465.2 Carbon replenishment device for large-scale cultivation of microalgae and its use and application) invented a well-type carbon replenishment device that directly supplements CO2 for the culture solution in an open pool, so that the culture solution is in the well-type Circulation is formed in the carbon replenishment device, which greatly prolongs the gas-liquid contact time, and the gas is supplied from the bottom of the trap carbon replenishment device, which greatly improves the CO 2 absorption rate. However, this carbon replenishment device increases the flow resistance of the fluid in the open pool, resulting in an increase in the power consumption of the impeller-driven fluid while maintaining the same flow rate, and in addition, the construction workload is relatively large.

发明内容 Contents of the invention

本发明的目的在于,为解决上述问题,提供一种用于开放池培养微藻的水平浸没罩式补碳装置。The object of the present invention is, in order to solve the above problems, to provide a horizontal immersion hood type carbon replenishing device for cultivating microalgae in an open pond.

本发明的另一目的是提供一种用于开放池培养微藻的补碳方法。Another object of the present invention is to provide a method for supplementing carbon for cultivating microalgae in open ponds.

本发明的构思为:直接在开放池底布设气体分布器,为了延长气液接触时间,在气体分布器上方设置浸没于培养液内的罩子,罩子沿培养液流动方向充分延长,使得气泡被封在罩子内,与培养液在罩子内一同流动时有充分的接触时间,从而提高气体的吸收率。The idea of the present invention is: directly arrange the gas distributor at the bottom of the open pool, in order to prolong the gas-liquid contact time, set a cover immersed in the culture solution above the gas distributor, and the cover is fully extended along the direction of the culture solution flow, so that the air bubbles are sealed. In the cover, there is sufficient contact time when the culture solution flows together in the cover, thereby improving the gas absorption rate.

本发明的用于开放池培养微藻的水平浸没罩式补碳装置,包括1个或2个以上的罩子1和气体分布器2,所述气体分布器2设置于开放池底部,所述罩子1罩于气体分布器2上方,罩子1呈两端开口的筒体,沿培养液流动方向布置,罩子1的两端口分别为培养液进口3和培养液出口4;其中,所述气体分布器2与罩子1的培养液出口4距离40厘米以上。The horizontal immersion hood type carbon replenishment device for cultivating microalgae in open ponds of the present invention includes one or more covers 1 and gas distributors 2, the gas distributors 2 are arranged at the bottom of the open pond, and the covers 1 is covered above the gas distributor 2, and the cover 1 is a cylinder with openings at both ends, arranged along the flow direction of the culture solution, and the two ports of the cover 1 are the culture solution inlet 3 and the culture solution outlet 4 respectively; wherein, the gas distributor 2 and the culture solution outlet 4 of the cover 1 are more than 40 centimeters away.

气体分布器2可以位于罩子1的培养液进口3或罩子其他部位的下方,只要保证从气体分布器2到罩子1的培养液出口4的距离在40厘米以上即可。优选气体分布器2位于罩子1的培养液进口3的下方。The gas distributor 2 can be located under the culture solution inlet 3 of the cover 1 or other parts of the cover, as long as the distance from the gas distributor 2 to the culture solution outlet 4 of the cover 1 is more than 40 cm. Preferably, the gas distributor 2 is located below the culture solution inlet 3 of the cover 1 .

根据本发明的补碳装置,优选气体分布器2与培养液出口4距离60~750厘米。为了施工方便并保证足够的二氧化碳吸收率,罩子1沿培养液流动方向的长度应保证气液接触时间在3秒~15秒,所以优选的从气体分布器2到罩子1的培养液出口4的距离是流道内培养液在3秒~15秒内的流动距离。一般开放池内培养液的流速为20~50厘米/秒,所以优选的从气体分布器2到罩子1的培养液出口4的距离是60~750厘米。According to the carbon replenishment device of the present invention, the distance between the gas distributor 2 and the culture solution outlet 4 is preferably 60-750 cm. In order to facilitate construction and ensure a sufficient carbon dioxide absorption rate, the length of the cover 1 along the direction of the flow of the culture solution should ensure that the gas-liquid contact time is 3 seconds to 15 seconds, so the preferred length from the gas distributor 2 to the culture solution outlet 4 of the cover 1 The distance is the flow distance of the culture solution in the channel within 3 seconds to 15 seconds. Generally, the flow velocity of the culture solution in the open pool is 20-50 cm/s, so the preferred distance from the gas distributor 2 to the culture solution outlet 4 of the cover 1 is 60-750 cm.

根据本发明的补碳装置,其中,所述罩子1直接固定于开放池底或架空设置于开放池底。According to the carbon replenishment device of the present invention, the cover 1 is directly fixed on the bottom of the open pool or installed overhead.

根据本发明的补碳装置,其中,所述罩子1的底部可以敞开也可以为封闭结构。According to the carbon replenishment device of the present invention, the bottom of the cover 1 can be open or closed.

根据本发明的补碳装置,其中,所述罩子1的主体呈半圆形筒体、弧形筒体、矩形筒体或梯形筒体。According to the carbon replenishment device of the present invention, the main body of the cover 1 is a semicircular cylinder, an arc cylinder, a rectangle cylinder or a trapezoid cylinder.

根据本发明的补碳装置,为了降低罩子1内的流体流动阻力,所述罩子1的培养液进口3和/或培养液出口4可以为锥形或喇叭形的扩口结构。According to the carbon replenishment device of the present invention, in order to reduce the fluid flow resistance in the cover 1, the culture solution inlet 3 and/or the culture solution outlet 4 of the cover 1 can be a cone-shaped or trumpet-shaped flared structure.

根据本发明的补碳装置,其中,所述罩子1高度为2~20厘米,以被培养液浸没为准。According to the carbon replenishment device of the present invention, the height of the cover 1 is 2-20 cm, subject to being submerged in the culture solution.

根据本发明的补碳装置,其中,所述罩子1宽度大于等于2厘米。每个罩子的宽度可以小到2厘米(如罩住一根气体分布管),大到接近开放池的宽度(如罩住多根气体分布管或多个气体分布器)。According to the carbon replenishing device of the present invention, the width of the cover 1 is greater than or equal to 2 cm. The width of each shroud can be as small as 2 cm (eg to cover a gas distribution tube) to as large as approximately the width of an open pool (eg to cover multiple gas distribution tubes or multiple gas distributors).

根据本发明的补碳装置,所述的气体分布器的气体分布面(板)为多孔材质,可以是管状气体分布器或联在输气管上的一个或多个气体分布头。可以是硬体的,如多孔陶瓷管或玻璃砂芯,或软体的,如市售的曝气软管或可变孔曝气软管。According to the carbon replenishing device of the present invention, the gas distribution surface (plate) of the gas distributor is made of porous material, which can be a tubular gas distributor or one or more gas distribution heads connected to the gas pipeline. They can be rigid, such as porous ceramic tubes or glass sand cores, or soft, such as commercially available aeration hoses or variable-porosity aeration hoses.

根据本发明的补碳装置,其中,所述2个以上的罩子1可以联体加工,形成联体结构。According to the carbon replenishment device of the present invention, the two or more covers 1 can be processed as a joint to form a joint structure.

所述的罩子1的壁厚为1毫米~10毫米。The wall thickness of the cover 1 is 1mm-10mm.

所述的罩子材质可以为塑料板、不锈钢板、木板等材料,能加工成型、有一定强度即可;可以为透明或不透明。The material of the cover can be plastic board, stainless steel board, wood board and other materials, which can be processed into shapes and have a certain strength; it can be transparent or opaque.

本发明的基于上述补碳装置的用于开放池培养微藻的补碳方法,其特征在于,将水平浸没罩式补碳装置沿开放池流道方向设置于开放池底部,使培养液浸没过罩子顶端;培养液在开放池原有的搅拌器9的推动下从罩子1的培养液进口3流入,在补碳装置内与气体分布器放出的CO2接触后从罩子1的培养液出口4流出。The carbon replenishment method for cultivating microalgae in an open pond based on the above carbon replenishment device of the present invention is characterized in that a horizontal immersion cover type carbon replenishment device is arranged on the bottom of the open pond along the direction of the flow path of the open pond, so that the culture solution is submerged The top of the cover; the culture solution flows in from the culture solution inlet 3 of the cover 1 under the push of the original agitator 9 of the open pool, and flows out from the culture solution outlet 4 of the cover 1 after being in contact with the CO2 released by the gas distributor in the carbon replenishing device .

所述开放池内的培养液流速为20~50厘米/秒。The flow velocity of the culture solution in the open pool is 20-50 cm/s.

所述水平浸没罩式补碳装置内的CO2流量,折合标准状况的纯CO2,为每米开放池宽度0.1~20升/分钟。The CO 2 flow rate in the horizontal immersion hood carbon replenishing device is equivalent to the pure CO 2 in standard conditions, and is 0.1-20 liters/minute per meter of open pool width.

所述的开放池内培养液的流动可以依靠开放池原有的搅拌器驱动实现,如叶轮或搅拌臂,搅拌器的材质可以为竹片、塑料、不锈钢、其它金属材料等。The flow of the culture solution in the open pool can be driven by the original agitator in the open pool, such as an impeller or an agitator arm, and the agitator can be made of bamboo chips, plastic, stainless steel, or other metal materials.

所述的开放池内培养液的深度可以是2~30厘米。The depth of the culture solution in the open pool can be 2-30 cm.

根据本发明的补碳方法,当采用的开放池内的培养液的深度较浅时,可以将开放池原有的搅拌器下降到搅拌器叶尖低于开放池底的位置,即,搅拌器9叶尖低于开放池底。According to the carbon replenishment method of the present invention, when the depth of the nutrient solution in the open pool used is relatively shallow, the original agitator of the open pool can be lowered to a position where the tip of the agitator is lower than the bottom of the open pool, that is, the 9 blades of the agitator are lower than the bottom of the open pool. Pointed below open pool bottom.

根据本发明的补碳方法,当采用的开放池内的培养液的深度较浅时,可以将开放池中拟安放补碳装置的池底区域挖出浅槽以安放补碳装置,即,将补碳装置安装于低于开放池底的位置。According to the carbon replenishing method of the present invention, when the depth of the culture solution in the open pool used is relatively shallow, shallow grooves can be dug out in the bottom area of the pool where the carbon replenishing device is to be placed in the open pool to place the carbon replenishing device, that is, the carbon replenishing device will be placed. The carbon unit is installed below the open pool floor.

所述的安放补碳装置的浅槽的底部可以是平底、带圆角的平底,也可以是半圆底;材质为水泥、塑料板、不锈钢板、砖或与开放池底同样的材料等。The bottom of the shallow tank for placing the carbon replenishing device can be flat bottom, flat bottom with rounded corners, or semicircular bottom; the material is cement, plastic plate, stainless steel plate, brick or the same material as the bottom of the open pool.

当气体分布器的外形是长形时,优选的气体分布器布设方式是将气体分布器的长的方向布设为与培养液流动方向一致。When the shape of the gas distributor is elongated, the preferred arrangement of the gas distributor is to arrange the long direction of the gas distributor to be consistent with the flow direction of the culture solution.

根据本发明的补碳方法,其中,所述CO2为净化烟道气、工业CO2气体、纯净的CO2气体或混合有CO2的空气中的一种或多种或液态CO2According to the carbon replenishing method of the present invention, the CO 2 is one or more of purified flue gas, industrial CO 2 gas, pure CO 2 gas or air mixed with CO 2 or liquid CO 2 .

用于培养微藻的培养基可以是本领域熟知的任意适合微藻生长的培养基,如Zarrouk培养基、SM培养基、ASP2培养基、BG-11培养基等,也可以是针对某种藻特殊需要的、培养过程需要CO2的培养基。The medium for cultivating microalgae can be any suitable medium for the growth of microalgae known in the art, such as Zarrouk medium, SM medium, ASP 2 medium, BG-11 medium, etc. Algae special needs, the culture process requires CO 2 medium.

本发明的水平浸没罩式补碳装置及补碳方法能够用于在开放池内大规模培养各种微藻过程中补充CO2,包括螺旋藻、栅藻、雨生红球藻、盐藻、小球藻、衣藻等各种微藻。The horizontal immersion hood type carbon replenishment device and carbon replenishment method of the present invention can be used to supplement CO 2 in the process of large-scale cultivation of various microalgae in open pools, including spirulina, Scenedesmus, Haematococcus pluvialis, salina, microalgae Various microalgae such as coccus and Chlamydomonas.

在开放池内培养微藻过程中,用CO2补碳时碳源利用率非常低的主要原因是培养液层比较浅,气液接触时间短,二氧化碳气体来不及被吸收即溢出。本发明的补碳装置不仅克服了上述缺点,而且比气罩法(李夜光,胡鸿钧,张良军,陈志祥。以二氧化碳为碳源工业化生产螺旋藻工艺技术的研究。武汉植物学研究,1996,14(4):349-356)吸收效率高,比槽式补碳(专利CN200610018771.9)操作方便,比阱式补碳装置(专利CN200510126465.2)降低了流体流动阻力、节省能耗。本发明,在开放池内培养微藻细胞时,能够有效利用二氧化碳进行补碳,大大降低了生产成本。In the process of culturing microalgae in an open pond, the main reason for the very low utilization rate of carbon sources when supplementing carbon with CO2 is that the culture solution layer is relatively shallow, the gas-liquid contact time is short, and the carbon dioxide gas overflows before it can be absorbed. The carbon replenishing device of the present invention not only overcomes the above-mentioned shortcoming, but also is better than the gas mask method (Li Yeguang, Hu Hongjun, Zhang Liangjun, Chen Zhixiang. Take carbon dioxide as the research on the carbon source industrialized production of spirulina technology. Wuhan Botany Research, 1996,14( 4): 349-356) has high absorption efficiency, and is more convenient to operate than the trough carbon supplement (patent CN200610018771.9), and reduces the fluid flow resistance and saves energy consumption than the trap carbon supplement (patent CN200510126465.2). In the present invention, when microalgae cells are cultivated in an open pool, carbon dioxide can be effectively used for carbon replenishment, and the production cost is greatly reduced.

附图说明 Description of drawings

图1为本发明的用于开放池培养微藻的水平浸没罩式补碳装置示意图。Fig. 1 is a schematic diagram of a horizontal immersion hood type carbon replenishment device for cultivating microalgae in an open pond according to the present invention.

图2为本发明的用于开放池培养微藻的水平浸没罩式补碳装置在开放池流道内的位置示意图。Fig. 2 is a schematic diagram of the position of the horizontal immersion hood-type carbon replenishing device for cultivating microalgae in an open pond in the flow channel of the open pond according to the present invention.

图3为本发明的用于开放池培养微藻的水平浸没罩式补碳装置使用时顺培养液流动方向视图。Fig. 3 is a view along the flow direction of the culture solution when the horizontal immersion hood carbon replenishment device for cultivating microalgae in an open pond of the present invention is in use.

图4为本发明的用于开放池培养微藻的水平浸没罩式补碳装置使用时侧视图。Fig. 4 is a side view of the horizontal immersion hood-type carbon replenishing device used for cultivating microalgae in an open pond according to the present invention when in use.

图5为本发明的补碳装置罩子的主体不同截面形状示意图(示罩子直接落在开放池底、示每个罩子下有一个或多个气体分布器、示罩子的截面形状)。Fig. 5 is a schematic diagram of different cross-sectional shapes of the main body of the cover of the carbon replenishment device of the present invention (showing that the cover falls directly on the bottom of the open pool, showing that there are one or more gas distributors under each cover, showing the cross-sectional shape of the cover).

图6为本发明的补碳装置的不同设置方式示意图(示罩子架空、示罩子底部敞开或封闭、示罩子联体、示气体分布器落地或架空)。Fig. 6 is a schematic diagram of different installation methods of the carbon replenishment device of the present invention (showing that the cover is overhead, showing that the bottom of the cover is open or closed, showing the combination of covers, and showing that the gas distributor is on the ground or overhead).

图7为本发明的补碳装置的罩子采用扩口结构示意图。Fig. 7 is a schematic diagram of a flared structure for the cover of the carbon replenishing device of the present invention.

图8为本发明的补碳装置用于培养液的深度较浅时与搅拌器叶尖低于开放池底的搅拌器配合使用示意图。Fig. 8 is a schematic diagram showing that the carbon replenishing device of the present invention is used in conjunction with an agitator whose blade tip is lower than the bottom of the open pool when the depth of the culture solution is relatively shallow.

图9为本发明的补碳装置安装于低于开放池底的位置顺培养液流动方向的视图。Fig. 9 is a view along the flow direction of the culture solution in which the carbon replenishing device of the present invention is installed at a position lower than the open pool bottom.

图10为本发明的补碳装置安装于低于开放池底的位置侧视图。Fig. 10 is a side view of the carbon replenishing device of the present invention installed at a position lower than the open pool bottom.

图11为本发明的补碳装置用于开放池培养微藻的总体布局示意图(俯视图)。Fig. 11 is a schematic diagram (top view) of the general layout of the carbon replenishing device of the present invention for cultivating microalgae in open ponds.

图12为利用本发明的补碳装置自动补碳的系统示意图。Fig. 12 is a schematic diagram of a system for automatic carbon replenishment using the carbon replenishment device of the present invention.

附图标记reference sign

1、罩子            2、气体分布器        3、培养液进口    4、培养液出口1. Cover 2. Gas distributor 3. Culture solution inlet 4. Culture solution outlet

5、培养液流动方向  6、开放池底部        7、开放池壁      8、微藻培养液液面5. The flow direction of the culture solution 6. The bottom of the open pool 7. The wall of the open pool 8. The liquid level of the microalgae culture solution

9、搅拌器          10、弧形容器         11、浅槽         12、pH传感器9. Agitator 10. Arc container 11. Shallow tank 12. pH sensor

13、控制装置       14、CO2气源          15、执行机构     16、流量计13. Control device 14. CO 2 gas source 15. Actuator 16. Flowmeter

17、压力表17. Pressure gauge

具体实施方式 Detailed ways

本发明的用于开放池培养微藻的水平浸没罩式补碳装置,包括1个或2个以上的罩子1和气体分布器2(图1、图6),所述气体分布器2设置于开放池底部6,所述罩子1罩于气体分布器2上方,该罩子1呈两端开口的筒体,沿培养液流动方向5布置,两端口分别为培养液进口3和培养液出口4(图2、图3);其中,所述气体分布器2与罩子1的培养液出口4距离40厘米以上。所述气体分布器2与罩子1的培养液出口4距离优选60~750厘米。罩子1可以直接固定于开放池底(图5)或架空设置于开放池底(图6,略去支撑装置),罩子1底部可以敞开也可以为封闭结构(图6)。罩子1的主体可以呈半圆形筒体、弧形筒体、矩形筒体或梯形筒体(图5)。为了降低罩子内的流体流动阻力,所述罩子1的培养液进口3和/或培养液出口4可以为锥形或喇叭形的扩口结构(图7)。罩子1高度为2~20厘米,以被微藻培养液液面8浸没为准。罩子1的宽度可以小到2厘米(如罩住一根气体分布管),可以大到接近开放池流道的宽度(即流道两侧开放池壁7的距离)(如罩住多根气体分布管或多个气体分布器)。所述2个以上的罩子1可以联体加工,形成联体结构(图6)。The horizontal immersion hood type carbon replenishing device for cultivating microalgae in open ponds of the present invention includes one or more hoods 1 and gas distributors 2 (Figure 1, Figure 6), and the gas distributor 2 is arranged on The bottom 6 of the pool is opened, and the cover 1 is covered above the gas distributor 2. The cover 1 is a cylinder with two ends open, arranged along the flow direction 5 of the culture solution, and the two ports are respectively the culture solution inlet 3 and the culture solution outlet 4 ( 2 and 3); wherein, the distance between the gas distributor 2 and the culture solution outlet 4 of the cover 1 is more than 40 cm. The distance between the gas distributor 2 and the culture solution outlet 4 of the cover 1 is preferably 60-750 cm. The cover 1 can be directly fixed on the bottom of the open pool (Figure 5) or installed overhead (Figure 6, the supporting device is omitted), and the bottom of the cover 1 can be open or closed (Figure 6). The main body of the cover 1 can be in the form of a semicircular cylinder, an arc cylinder, a rectangle cylinder or a trapezoid cylinder (Fig. 5). In order to reduce the fluid flow resistance in the cover, the culture solution inlet 3 and/or the culture solution outlet 4 of the cover 1 can be a cone-shaped or trumpet-shaped flared structure ( FIG. 7 ). The height of the cover 1 is 2 to 20 centimeters, subject to being submerged in the liquid level 8 of the microalgae culture solution. The width of the cover 1 can be as small as 2 cm (such as covering a gas distribution pipe), and can be as large as the width of the flow channel of the open pool (that is, the distance between the open pool walls 7 on both sides of the flow channel) (such as covering a plurality of gas pipes) distribution pipe or multiple gas distributors). The two or more covers 1 can be combined to form a combined structure ( FIG. 6 ).

本发明的用于开放池培养微藻的补碳方法,其特征在于,在开放池内沿流道方向设置一组或多组水平浸没罩式补碳装置,每组包含一个或多个水平浸没罩式补碳装置,每个水平浸没罩式补碳装置含一个顺培养液流动方向的罩子和被其罩住的一个或多个气体分布器,气体分布器优选设置在罩子的培养液进口3处,总体布局见图11,水平浸没罩式补碳装置的组数、每组含水平浸没罩式补碳装置的个数、每个罩子下的气体分布器的个数依据单个水平浸没罩式补碳装置的补碳速率、开放池的大小、培养对象的生长速率及工艺要求而设定。培养液在搅拌器(本领域常规使用的搅拌器是叶轮)的推动下在开放池内流动时,部分培养液由罩子的培养液进口3流入水平浸没罩式补碳装置中,与气体分布器放出的被封在罩子下方的含二氧化碳的气体接触,流经罩子下方的空间,再由水平浸没罩式补碳装置的培养液出口4流出,这样大大延长了气液接触时间;另一方面,含二氧化碳的气体通过气体分布器后,变成很小的气泡,气液接触面积急剧增大,这样就大大提高了二氧化碳的吸收率。The carbon replenishing method for cultivating microalgae in an open pool of the present invention is characterized in that one or more groups of horizontal immersion hood carbon replenishment devices are arranged along the direction of the flow channel in the open pool, and each group includes one or more horizontal immersion hoods Each horizontal immersion hood carbon replenishment device contains a cover along the flow direction of the culture solution and one or more gas distributors covered by it. The gas distributor is preferably arranged at the culture solution inlet 3 of the cover. , the overall layout is shown in Figure 11. The number of groups of horizontal immersion hood carbon replenishment devices, the number of horizontal immersion hood carbon replenishment devices in each group, and the number of gas distributors under each hood are based on the number of horizontal immersion hood carbon replenishment devices. The carbon replenishment rate of the carbon device, the size of the open pool, the growth rate of the culture object and the process requirements are set. When the culture solution flows in the open pool driven by the agitator (the agitator conventionally used in this field is an impeller), part of the culture solution flows into the horizontal submerged hood carbon replenishment device from the culture solution inlet 3 of the cover, and is released from the gas distributor. The carbon dioxide-containing gas that is sealed under the hood contacts, flows through the space below the hood, and then flows out from the culture solution outlet 4 of the horizontal immersion hood-type carbon replenishing device, which greatly prolongs the gas-liquid contact time; on the other hand, the gas containing After the carbon dioxide gas passes through the gas distributor, it becomes very small bubbles, and the gas-liquid contact area increases sharply, which greatly improves the absorption rate of carbon dioxide.

培养液的流动可以依靠开放池原有的的搅拌器驱动实现,如叶轮或搅拌臂,搅拌器的材质可以为竹片、塑料、不锈钢、其它金属材料等。The flow of the culture medium can be driven by the original agitator in the open pool, such as impeller or stirring arm, and the material of the agitator can be bamboo chips, plastic, stainless steel, or other metal materials.

使用该水平浸没罩式补碳装置时的开放池内的培养液流速一般为20~50厘米/秒,CO2流量(折合标准状况的纯CO2)为每米开放池宽度上0.1~20升/分钟。When using the horizontal immersion hood carbon replenishing device, the flow rate of the culture solution in the open pool is generally 20-50 cm/s, and the CO 2 flow rate (pure CO 2 equivalent to standard conditions) is 0.1-20 liters/meter per meter of open pool width. minute.

所述的开放池内的培养液的深度可以是2~30厘米。The depth of the culture solution in the open pool can be 2-30 cm.

当采用的开放池内的培养液的深度较浅时,可以将开放池原有的搅拌器9设置在弧形容器10的上方,搅拌器叶尖低于开放池底(图8);可以将开放池中拟安放补碳装置的池底区域挖出浅槽11以安放补碳装置,即,将补碳装置安装于低于开放池底的位置(图9、图10)。所述的安放补碳装置的浅槽11的底部可以是平底、带圆角的平底,也可以是半圆底(图9);材质为水泥、塑料板、不锈钢板、砖或与开放池底同样的材料等。When the depth of the nutrient solution in the open pool adopted is relatively shallow, the original stirrer 9 of the open pool can be arranged above the arc-shaped container 10, and the tip of the stirrer is lower than the bottom of the open pool (Fig. 8); A shallow groove 11 is dug out in the bottom area of the pool where the carbon replenishing device is to be placed to place the carbon replenishing device, that is, the carbon replenishing device is installed at a position lower than the open pool bottom (Fig. 9, Fig. 10). The bottom of the shallow tank 11 for placing the carbon replenishing device can be a flat bottom, a flat bottom with rounded corners, or a semicircular bottom (Figure 9); the material is cement, plastic plate, stainless steel plate, brick or the same as the bottom of the open pool. materials etc.

实施例1Example 1

如图11所示,在跑道式培养池(最常见的一种开放池,简称跑道池)内进行螺旋藻培养。跑道池流道周长70米、宽3米,搅拌器9为由一根转轴带动的4组钢制叶轮,每个叶轮有4个叶片,相互间隔90度角,相邻叶轮的叶片交错45度角,转轴由交流电机及减速机带动,搅拌器9的自转半径为50厘米。As shown in Figure 11, Spirulina is cultivated in a track-type culture pool (the most common open pool, referred to as the track pool). The circumference of the runway pool flow channel is 70 meters and the width is 3 meters. The agitator 9 is 4 sets of steel impellers driven by a rotating shaft. Each impeller has 4 blades, which are spaced at an angle of 90 degrees. The blades of adjacent impellers are staggered by 45. degree angle, the rotating shaft is driven by an AC motor and a reducer, and the rotation radius of the agitator 9 is 50 centimeters.

在跑道池内沿流道方向设置一组6个水平浸没罩式补碳装置,每个水平浸没罩式补碳装置含一个顺培养液流动方向的罩子1和被其罩住的一个气体分布器2。每个罩子由1毫米厚的不锈钢板制成,罩子的主体截面形状为半圆,每个罩子长度400厘米,宽10厘米,高5厘米。气体分布器2为微孔橡胶膜曝气管,长50厘米,其外径16毫米,内径10毫米,孔径约为30~60微米,顺培养液流动方向设置在罩子下方的培养液进口0~50厘米之间、径向位置居中。培养液被搅拌器9推动顺流道流动,部分培养液进入补碳装置的培养液进口3,与气体分布器2放出的气泡接触,流经罩子1下方的空间,流出补碳装置的培养液出口4,与未进入补碳装置的培养液混合后在流道内继续循环流动。A group of 6 horizontal immersion hood carbon replenishment devices are set along the flow path in the runway pool, and each horizontal immersion hood carbon replenishment device includes a cover 1 along the flow direction of the culture solution and a gas distributor 2 covered by it . Each cover is made of a 1mm thick stainless steel plate, the main section of the cover is semicircular in shape, and each cover is 400 cm long, 10 cm wide, and 5 cm high. The gas distributor 2 is a microporous rubber membrane aeration tube, 50 cm long, with an outer diameter of 16 mm, an inner diameter of 10 mm, and an aperture of about 30 to 60 microns. Between 50 cm, the radial position is centered. The culture solution is pushed by the agitator 9 to flow along the flow channel, part of the culture solution enters the culture solution inlet 3 of the carbon replenishment device, contacts with the air bubbles released from the gas distributor 2, flows through the space under the cover 1, and flows out of the culture solution of the carbon replenishment device Outlet 4, after being mixed with the culture solution that has not entered the carbon replenishment device, it continues to circulate in the flow channel.

补碳采用自动控制,自动控制方法见申请号CN200410009360.4的专利,实施方案系统参见图12。其中,pH传感器12为市售pH电极,控制装置13为带开关控制的pH计,CO2气源14为来自钢瓶的纯净的二氧化碳气体,执行机构15是两位常闭电磁阀(通径8毫米)。依据培养液的pH值控制二氧化碳进气阀门(执行机构15)的开启与关闭。CO2气体的流量及压力通过流量计16和压力表17监测。The carbon replenishment adopts automatic control, the automatic control method is shown in the patent of application number CN200410009360.4, and the implementation scheme system is shown in Figure 12. Among them, the pH sensor 12 is a commercially available pH electrode, the control device 13 is a pH meter with switch control, the CO2 gas source 14 is pure carbon dioxide gas from a cylinder, and the actuator 15 is a two-position normally closed solenoid valve (diameter 8 mm). The opening and closing of the carbon dioxide inlet valve (actuator 15) is controlled according to the pH value of the culture solution. The flow and pressure of the CO gas are monitored by a flow meter 16 and a pressure gauge 17.

藻种为钝顶螺旋藻(Spirulina Platensis),来自中国科学院水生生物研究所淡水藻种库,编号439,培养基为Zarrouk培养基,其中碳酸氢钠的初始浓度为0.05mol/L。跑道池内培养液平均深度15厘米,藻细胞接种密度0.40g(干重)/L。pH的控制范围设定为9.6~9.7,当培养液的pH升高到9.6时启动自动补碳,每个气体分布器的二氧化碳气体的流量(执行机构15开)为1升/分钟(纯二氧化碳,标况)。调节电机的转速使得跑道池内培养液的流速为25厘米/秒左右。The algal species is Spirulina Platensis, which comes from the freshwater algae species bank of the Institute of Hydrobiology, Chinese Academy of Sciences, No. 439. The medium is Zarrouk medium, and the initial concentration of sodium bicarbonate is 0.05mol/L. The average depth of the culture medium in the raceway pool is 15 cm, and the inoculation density of algae cells is 0.40 g (dry weight)/L. The pH control range is set at 9.6 to 9.7. When the pH of the culture medium rises to 9.6, automatic carbon replenishment is started, and the flow rate of carbon dioxide gas in each gas distributor (executor 15K) is 1 liter/min (pure carbon dioxide , standard condition). Adjust the rotation speed of the motor so that the flow rate of the culture solution in the raceway pool is about 25 cm/s.

每天定时检测其他营养盐的浓度并及时补充,并补充少量水以弥补水的蒸发损耗。持续培养6天,藻细胞密度达到0.70g(干重)/L,单位面积藻细胞的产量达到13.3g(干重)/m2.d。获得螺旋藻藻粉的常规成分、氨基酸、脂肪酸以及类胡萝卜素的组成及含量与文献报道基本一致。经过物料衡算得出钢瓶二氧化碳的利用率为92%。Regularly detect the concentration of other nutrients every day and replenish them in time, and add a small amount of water to make up for the evaporation loss of water. After continuous cultivation for 6 days, the algal cell density reaches 0.70g (dry weight)/L, and the yield of algal cells per unit area reaches 13.3g (dry weight)/m 2 .d. The composition and content of conventional components, amino acids, fatty acids and carotenoids obtained from Spirulina algae powder are basically consistent with those reported in the literature. Through material balance calculation, the utilization rate of carbon dioxide in the steel cylinder is 92%.

实施例2.Example 2.

其他同实施例1。在开放池内培养小球藻,培养液是以NaNO3为氮源的BG-11培养基。跑道池内培养液平均深度12厘米。藻细胞接种密度0.5g(干重)/L。pH的控制范围设定为7.5~7.6。每个气体分布器的二氧化碳气体的流量(执行机构15开)为0.5升/分钟(纯二氧化碳,标况)。跑道池内培养液的流速为30厘米/秒左右。持续培养6天,钢瓶二氧化碳的利用率为90%。Others are the same as embodiment 1. Chlorella was cultivated in an open pool, and the culture medium was BG-11 medium with NaNO3 as nitrogen source. The average depth of the culture medium in the runway pool is 12 cm. Algal cell inoculation density 0.5g (dry weight) / L. The control range of pH was set at 7.5-7.6. The flow rate of carbon dioxide gas in each gas distributor (actuator 15K) is 0.5 L/min (pure carbon dioxide, standard condition). The flow velocity of the culture solution in the raceway pool is about 30 cm/s. After continuous cultivation for 6 days, the utilization rate of carbon dioxide in the cylinder was 90%.

实施例3.Example 3.

其他同实施例1。每个罩子长度800厘米,宽6厘米,高3厘米。跑道池内培养液平均深度10厘米。藻细胞接种密度0.6g(干重)/L。pH的控制范围设定为9.5~9.6。每个气体分布器的二氧化碳气体的流量(执行机构15开)为1升/分钟(纯二氧化碳,标况)。跑道池内培养液的流速为50厘米/秒左右。持续培养6天,钢瓶二氧化碳的利用率为98%。Others are the same as embodiment 1. Each cover is 800 cm long, 6 cm wide and 3 cm high. The average depth of the culture medium in the runway pool is 10 cm. The algae cell inoculation density is 0.6g (dry weight)/L. The control range of pH is set at 9.5-9.6. The flow rate of carbon dioxide gas in each gas distributor (actuator 15K) is 1 liter/minute (pure carbon dioxide, standard condition). The flow velocity of the culture solution in the raceway pool is about 50 cm/s. After continuous cultivation for 6 days, the utilization rate of carbon dioxide in the steel cylinder was 98%.

实施例4.Example 4.

其他同实施例1。设置一组3个水平浸没罩式补碳装置,每个水平浸没罩式补碳装置含1个顺培养液流动方向的罩子和被其罩住的4个气体分布器。罩子的主体截面形状为弧形,每个罩子长度200厘米,宽40厘米,高10厘米。在开放池内培养小球藻,培养液是以NaNO3为氮源的BG-11培养基。跑道池内培养液平均深度20厘米。藻细胞接种密度0.3g(干重)/L。pH的控制范围设定为7.5~7.6。每个气体分布器的二氧化碳气体的流量(执行机构15开)为0.5升/分钟(纯二氧化碳,标况)。跑道池内培养液的流速为25厘米/秒左右。持续培养6天,钢瓶二氧化碳的利用率为86%。Others are the same as embodiment 1. Set up a group of 3 horizontal immersion hood carbon replenishment devices, each horizontal immersion hood carbon replenishment device contains a hood along the flow direction of the culture solution and 4 gas distributors covered by it. The main section of the cover is arc-shaped, and each cover is 200 centimeters in length, 40 centimeters in width and 10 centimeters in height. Chlorella was cultivated in an open pool, and the culture medium was BG-11 medium with NaNO3 as nitrogen source. The average depth of the culture medium in the runway pool is 20 cm. Algal cell inoculation density 0.3g (dry weight) / L. The control range of pH was set at 7.5-7.6. The flow rate of carbon dioxide gas in each gas distributor (actuator 15K) is 0.5 L/min (pure carbon dioxide, standard condition). The flow velocity of the culture solution in the raceway pool is about 25 cm/s. After continuous cultivation for 6 days, the utilization rate of carbon dioxide in the steel cylinder was 86%.

实施例5.Example 5.

其他同实施例1。在搅拌器下方挖出半径为52厘米、深度10厘米的半圆弧形槽,使搅拌器的叶尖下降到低于跑道池底8厘米。每个水平浸没罩式补碳装置含1个顺培养液流动方向的罩子和被其罩住的2个气体分布器。罩子的主体截面形状为弧形,每个罩子长度200厘米,宽15厘米,高3厘米。每个补碳装置下方的池底区域挖出2厘米深的平底斜坡的浅槽,每个罩子及气体分布器直接设置于浅槽的平底上(图9、图10)。在开放池内培养栅藻,培养液是以NaNO3为氮源的BG-11培养基。跑道池内培养液平均深度5厘米。藻细胞接种密度1.2g(干重)/L。pH的控制范围设定为7.4~7.5。每个气体分布器的二氧化碳气体的流量(执行机构15开)为0.5升/分钟(纯二氧化碳,标况)。跑道池内培养液的流速为25厘米/秒左右。持续培养6天,钢瓶二氧化碳的利用率为85%。Others are the same as embodiment 1. Dig out a semicircle arc-shaped groove with a radius of 52 centimeters and a depth of 10 centimeters below the stirrer, so that the blade tip of the stirrer drops to 8 centimeters below the bottom of the runway pool. Each horizontal immersion hood carbon replenishment device contains a hood along the flow direction of the culture solution and 2 gas distributors covered by it. The main section of the cover is arc-shaped, and each cover is 200 centimeters in length, 15 centimeters in width and 3 centimeters in height. A 2cm-deep shallow groove with a flat bottom slope is dug in the pool bottom area below each carbon replenishing device, and each cover and gas distributor are directly placed on the flat bottom of the shallow groove (Figure 9, Figure 10). Scenedesmus was cultured in an open pond, and the culture medium was BG-11 medium with NaNO 3 as the nitrogen source. The average depth of the culture medium in the runway pool is 5 cm. The algae cell inoculation density was 1.2g (dry weight)/L. The control range of pH was set at 7.4-7.5. The flow rate of carbon dioxide gas in each gas distributor (actuator 15K) is 0.5 L/min (pure carbon dioxide, standard condition). The flow velocity of the culture solution in the raceway pool is about 25 cm/s. After continuous cultivation for 6 days, the utilization rate of carbon dioxide in the cylinder was 85%.

实施例6.Example 6.

其他同实施例1。在搅拌器下方挖出半径为52厘米、深度10厘米的半圆弧形槽,使搅拌器的叶尖下降到低于跑道池底8厘米。每个水平浸没罩式补碳装置含1个顺培养液流动方向的罩子和被其罩住的2个气体分布器。罩子的主体截面形状为弧形,每个罩子长度200厘米,宽10厘米,高2厘米。每个补碳装置下方的池底区域挖出3厘米深的平底斜坡的浅槽,每个罩子及气体分布器架空1厘米设置于浅槽的平底上(图9、图10、图6)。跑道池内培养液平均深度3厘米。藻细胞接种密度2g(干重)/L。pH的控制范围设定为9.7~9.8。每个气体分布器的二氧化碳气体的流量(执行机构15开)为0.5升/分钟(纯二氧化碳,标况)。跑道池内培养液的流速为25厘米/秒左右。持续培养6天,钢瓶二氧化碳的利用率为88%。Others are the same as embodiment 1. Dig out a semicircle arc-shaped groove with a radius of 52 centimeters and a depth of 10 centimeters below the stirrer, so that the blade tip of the stirrer drops to 8 centimeters below the bottom of the runway pool. Each horizontal immersion hood carbon replenishment device contains a hood along the flow direction of the culture solution and 2 gas distributors covered by it. The main section of the cover is arc-shaped, and each cover is 200 centimeters in length, 10 centimeters in width and 2 centimeters in height. A 3cm-deep flat-bottomed slope shallow groove is dug in the pool bottom area below each carbon replenishment device, and each cover and gas distributor is set on the flat bottom of the shallow groove 1cm above the ground (Fig. 9, Fig. 10, Fig. 6). The average depth of the culture medium in the runway pool is 3 cm. Algal cell inoculation density 2g (dry weight) / L. The control range of pH was set at 9.7-9.8. The flow rate of carbon dioxide gas in each gas distributor (actuator 15K) is 0.5 L/min (pure carbon dioxide, standard condition). The flow velocity of the culture solution in the raceway pool is about 25 cm/s. After continuous cultivation for 6 days, the utilization rate of carbon dioxide in the steel cylinder was 88%.

实施例7.Example 7.

其他同实施例1。罩子的主体截面形状为梯形,每个罩子长度100厘米,宽15厘米,高15厘米。气体分布器是直径65mm的可变孔曝气软管,长40厘米,顺培养液流动方向设置在罩子下方的培养液进口0~40厘米之间。跑道池内培养液平均深度25厘米。藻细胞接种密度0.24g(干重)/L。pH的控制范围设定为9.8~9.9。每个气体分布器的二氧化碳气体的流量(执行机构15开)为1升/分钟(纯二氧化碳,标况)。跑道池内培养液的流速为20厘米/秒左右。持续培养6天,钢瓶二氧化碳的利用率为79%。Others are the same as embodiment 1. The main body section shape of the cover is trapezoidal, and each cover is 100 centimeters in length, 15 centimeters in width, and 15 centimeters in height. The gas distributor is a variable-porous aeration hose with a diameter of 65 mm and a length of 40 centimeters, which is arranged between 0 and 40 centimeters of the culture solution inlet below the cover along the flow direction of the culture solution. The average depth of the culture medium in the runway pool is 25 cm. The algae cell inoculation density was 0.24g (dry weight)/L. The control range of pH was set at 9.8-9.9. The flow rate of carbon dioxide gas in each gas distributor (actuator 15K) is 1 liter/minute (pure carbon dioxide, standard condition). The flow velocity of the culture solution in the raceway pool is about 20 cm/s. After continuous cultivation for 6 days, the utilization rate of carbon dioxide in the steel cylinder was 79%.

实施例8.Example 8.

其他同实施例1。每个水平浸没罩式补碳装置含1个顺培养液流动方向的罩子和被其罩住的2个气体分布器。罩子的主体截面形状为矩形,每个罩子长度50厘米,宽20厘米,高20厘米。气体分布器是直径30毫米的砂芯,高70毫米,垂直于培养液流动方向并排设置在罩子下方的培养液进口5~10厘米之间。跑道池内培养液平均深度30厘米。藻细胞接种密度0.2g(干重)/L。pH的控制范围设定为9.9~10.0。每个气体分布器的二氧化碳气体的流量(执行机构15开)为0.5升/分钟(纯二氧化碳,标况)。跑道池内培养液的流速为15厘米/秒左右。持续培养6天,钢瓶二氧化碳的利用率为75%。Others are the same as embodiment 1. Each horizontal immersion hood carbon replenishment device contains a hood along the flow direction of the culture solution and 2 gas distributors covered by it. The main body section shape of the cover is rectangular, and each cover is 50 centimeters in length, 20 centimeters in width, and 20 centimeters in height. The gas distributor is a sand core with a diameter of 30 mm and a height of 70 mm, and is arranged side by side perpendicular to the flow direction of the culture solution between 5 and 10 cm of the culture solution inlet below the cover. The average depth of the culture medium in the runway pool is 30 cm. Algal cell inoculation density 0.2g (dry weight) / L. The control range of pH was set at 9.9-10.0. The flow rate of carbon dioxide gas in each gas distributor (actuator 15K) is 0.5 L/min (pure carbon dioxide, standard condition). The flow velocity of the culture solution in the raceway pool is about 15 cm/s. After continuous cultivation for 6 days, the utilization rate of carbon dioxide in the cylinder was 75%.

Claims (15)

1. a horizontal submergence bell-type carbon compensator of cultivating micro-algae for open pond, comprise 1 or 2 above cover (1) and gas distributors (2), it is characterized in that, described gas distributor (2) is arranged at bottom, open pond, described cover (1) is the cylindrical shell of both ends open, along nutrient solution flow direction, arrange, the two-port of cover (1) is respectively nutrient solution import (3) and nutrient solution outlet (4); At the bottom of described cover (1) is directly fixed on open pond or built on stilts be arranged at open pond at the bottom of; Wherein, described cover (1) bottom is open, covers in gas distributor (2) top; Or be enclosed construction bottom described cover (1), described gas distributor (2) is positioned at the inside of cover (1); Described gas distributor (2) exports (4) distance more than 40 centimetres with the nutrient solution of cover (1).
2. carbon compensator according to claim 1, is characterized in that, described gas distributor (2) exports 60~750 centimetres of (4) distances with the nutrient solution of cover (1).
3. carbon compensator according to claim 1, is characterized in that, main body semicircular in shape cylindrical shell, arc cylindrical shell, rectangle cylindrical shell or the trapezoidal cylindrical shell of described cover (1).
4. carbon compensator according to claim 1, is characterized in that, the two-port of described cover (1) is taper or flaring flaring structure.
5. carbon compensator according to claim 1, is characterized in that, described cover (1) is highly 2~20 centimetres.
6. carbon compensator according to claim 1, is characterized in that, described cover (1) width is more than or equal to 2 centimetres.
7. carbon compensator according to claim 1, is characterized in that, described 2 above covers (1) form conjuncted structure.
8. the benefit carbon method of cultivating the horizontal submergence bell-type carbon compensator of micro-algae for open pond based on claim 1, it is characterized in that, horizontal submergence bell-type carbon compensator is arranged to bottom, open pond along open pond runner direction, make nutrient solution submergence cross cover top, nutrient solution nutrient solution import (3) from cover (1) under the promotion of the open original agitator in pond (9) flows into, the CO emitting with gas distributor in carbon compensator 2after contact, from nutrient solution outlet (4), flow out;
Nutrient solution flow velocity in described open pond is 20~50 cels;
CO in described horizontal submergence bell-type carbon compensator 2flow, amounts to the pure CO of the normal conditions 2, be 0.1~20 liter/min of every meter of open pond width.
9. benefit carbon method according to claim 8, is characterized in that, in described open pond, medium depth is 2~30 centimetres.
10. benefit carbon method according to claim 8, is characterized in that, described agitator blade tip is lower than at the bottom of opening pond.
11. benefit carbon methods according to claim 8, is characterized in that, described horizontal submergence bell-type carbon compensator is arranged in the shallow slot of bottom, open pond.
12. benefit carbon methods according to claim 11, is characterized in that, described shallow slot bottom is for flat or with the flat or Semi round bottom of fillet.
13. benefit carbon methods according to claim 8, is characterized in that described CO 2for purifying flue gas, industrial CO 2gas, pure CO 2gas or be mixed with CO 2airborne one or more or liquid CO 2.
14. benefit carbon methods according to claim 8, is characterized in that, the substratum of the micro-algae of described cultivation is Zarrouk substratum, SM substratum, ASP 2substratum or BG-11 substratum.
15. benefit carbon methods according to claim 8, is characterized in that, described micro-algae is spirulina, grid algae, Haematocoocus Pluvialls, salt algae, chlorella or chlamydomonas.
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