CN118207066B - Culture unit, culture device and culture method for spirulina - Google Patents
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Abstract
Description
技术领域Technical Field
本发明属于螺旋藻养殖技术领域,具体涉及一种盐泽螺旋藻培养单元、培养装置及培养方法。The invention belongs to the technical field of spirulina cultivation, and in particular relates to a salt-water spirulina cultivation unit, a cultivation device and a cultivation method.
背景技术Background Art
这里的陈述仅提供与本发明相关的背景技术,而不必然地构成现有技术。The statements herein merely provide background information related to the present invention and do not necessarily constitute prior art.
螺旋藻是一种由单细胞或多细胞组成的丝状原核生物,是已成功实现规模化生产的微藻之一。目前商业化应用的螺旋藻藻种主要为钝顶螺旋藻和极大螺旋藻,而盐泽螺旋藻生长速度快、光合效率强、蛋白含量高,具有扩大规模生产的潜力。寻找适合盐泽螺旋藻的养殖模式,扩大培养规模是至关重要的。Spirulina is a filamentous prokaryotic organism composed of single cells or multiple cells. It is one of the microalgae that has been successfully mass-produced. The main species of Spirulina currently used commercially are Spirulina platensis and Spirulina maxima. However, Spirulina salina has a fast growth rate, high photosynthetic efficiency, and high protein content, and has the potential for large-scale production. It is crucial to find a suitable cultivation model for Spirulina salina and expand the cultivation scale.
螺旋藻规模化生产多采用开放式养殖池进行培养,占地面积大,人工操作难,易引起生物污染;培养装置多采用曝气、搅拌等方式进行扰动,存在能耗高、设备复杂、维护困难等问题,不利于规模化生产和成本控制。Large-scale production of spirulina mostly uses open culture ponds, which occupy a large area, are difficult to operate manually, and are prone to biological contamination. The culture devices mostly use aeration, stirring and other methods for disturbance, which have problems such as high energy consumption, complex equipment, and difficult maintenance, which is not conducive to large-scale production and cost control.
盐泽螺旋藻在低光照强度时生长良好,但光会随着水的深度增加而迅速衰减,底层的盐泽螺旋藻难以获得充足的光照以保证其光合作用,常用的促使微藻在培养容器内均匀分布的分散方法,如曝气、搅拌等,会对盐泽螺旋藻产生机械损伤,不适合盐泽螺旋藻的规模化生产。Spirulina grows well under low light intensity, but the light will decay rapidly with the increase of water depth. It is difficult for the Spirulina at the bottom to obtain sufficient light to ensure its photosynthesis. The commonly used dispersion methods to promote the uniform distribution of microalgae in the culture container, such as aeration and stirring, will cause mechanical damage to Spirulina and are not suitable for large-scale production of Spirulina.
发明内容Summary of the invention
针对现有技术存在的不足,本发明的目的是提供一种盐泽螺旋藻培养单元、培养装置及培养方法,以解决现有技术中盐泽螺旋藻扩大规模困难的问题。In view of the shortcomings of the prior art, the purpose of the present invention is to provide a culture unit, a culture device and a culture method for Spirulina salina to solve the problem of difficulty in scaling up Spirulina salina in the prior art.
为了实现上述目的,本发明是通过如下的技术方案来实现:In order to achieve the above object, the present invention is implemented through the following technical solutions:
第一方面,本发明提供一种盐泽螺旋藻培养单元,包括反应器主体、反应器顶盖和培养架,其中,In a first aspect, the present invention provides a culture unit for Spirulina salizawa, comprising a reactor body, a reactor top cover and a culture rack, wherein:
所述反应器主体为顶部开放的培养箱;The reactor body is an incubator with an open top;
反应器顶盖可拆卸盖合于反应器主体的顶部,反应器顶盖由透明材料制成,且反应器顶盖上设置有若干通孔;The reactor top cover is detachably covered on the top of the reactor body, the reactor top cover is made of a transparent material, and a plurality of through holes are arranged on the reactor top cover;
光源安装在培养架上,且位于反应器顶盖的上方。The light source is installed on the culture rack and is located above the top cover of the reactor.
在一些实施例中,反应器顶盖上设置有两组通孔,两组通孔相对设置于反应器顶盖的两侧。In some embodiments, two groups of through holes are disposed on the reactor top cover, and the two groups of through holes are disposed oppositely on two sides of the reactor top cover.
优选的,每组通孔的数量为2-5个,每个通孔直径为2-4cm。Preferably, the number of through holes in each group is 2-5, and the diameter of each through hole is 2-4 cm.
在一些实施例中,反应器主体的长度为35-95cm,宽度为25-45cm,深为2-10cm。In some embodiments, the reactor body has a length of 35-95 cm, a width of 25-45 cm, and a depth of 2-10 cm.
优选的,反应器内培养液的深度为4-5cm。Preferably, the depth of the culture solution in the reactor is 4-5 cm.
优选的,反应器主体的横截面积为900-2000cm2。Preferably, the cross-sectional area of the reactor body is 900-2000 cm 2 .
在一些实施例中,所述光源在反应器主体的上方均匀分布。In some embodiments, the light sources are evenly distributed above the reactor body.
优选的,所述光源的亮度为2500-3500lux。Preferably, the brightness of the light source is 2500-3500 lux.
第二方面,本发明提供一种盐泽螺旋藻培养装置,所述培养架为多层培养架,每层培养架上放置有至少一个培养单元;可根据需要调整反应器主体的数量,对反应器主体、反应器顶盖、光源、盐泽螺旋藻培养架进行组装,实现对盐泽螺旋藻的规模化培养。In a second aspect, the present invention provides a salt-water Spirulina cultivation device, wherein the cultivation rack is a multi-layer cultivation rack, and at least one cultivation unit is placed on each layer of the cultivation rack; the number of reactor bodies can be adjusted as needed, and the reactor body, reactor top cover, light source, and salt-water Spirulina cultivation rack can be assembled to achieve large-scale cultivation of salt-water Spirulina.
第三方面,本发明提供采用所述盐泽螺旋藻培养单元或所述盐泽螺旋藻培养装置的盐泽螺旋藻培养方法,包括如下步骤:In a third aspect, the present invention provides a method for cultivating Spirulina salizae using the Spirulina salizae cultivation unit or the Spirulina salizae cultivation device, comprising the following steps:
向海水中添加体积分数为1‰-2‰的味精废水,制备得到培养基溶液;其中,味精废水和海水使用前分别采用6层纱布和0.45微米滤膜进行过滤,味精废水的总氮、总磷、氨氮为55.26,3.53,47.51g/L,海水的盐度为2.36%;Adding monosodium glutamate wastewater with a volume fraction of 1‰-2‰ to seawater to prepare a culture medium solution; wherein the monosodium glutamate wastewater and seawater are filtered by 6 layers of gauze and 0.45 micron filter membrane respectively before use, the total nitrogen, total phosphorus and ammonia nitrogen of the monosodium glutamate wastewater are 55.26, 3.53 and 47.51 g/L, and the salinity of the seawater is 2.36%;
将培养基溶液加入反应器主体中,使培养基溶液的深度为4-5cm,并向其中加入盐泽螺旋藻,使其初始浓度为0.05-0.15g/L;Add the culture medium solution into the reactor body to a depth of 4-5 cm, and add Spirulina salizawa thereto to an initial concentration of 0.05-0.15 g/L;
打开光源进行培养,初始光照设定在2500-3500lux,培养过程中所需的二氧化碳和释放的氧气通过反应器顶盖上的通孔进行交换;Turn on the light source for cultivation, with the initial illumination set at 2500-3500 lux. The carbon dioxide required and the released oxygen during the cultivation process are exchanged through the through holes on the top cover of the reactor;
培养设定时间后收获。Harvest after a set period of culture.
上述本发明的一种或多种实施例取得的有益效果如下:The beneficial effects achieved by one or more embodiments of the present invention are as follows:
(1)通过深入研究反应器培养液深度和面积对盐泽螺旋藻生长的影响,优化设计出适合其生长的培养装置,使培养条件更加符合盐泽螺旋藻的生长需求,显著提高了培养效率。(1) Through in-depth research on the effects of reactor culture medium depth and area on the growth of Spirulina, we optimized the design of a culture device suitable for its growth, making the culture conditions more in line with the growth requirements of Spirulina and significantly improving the culture efficiency.
(2)培养装置无传统的曝气、搅拌等动力条件和复杂的设备运转,在维持盐泽螺旋藻生长所需环境的同时,减少了不必要的能源消耗,降低了培养的运营成本;(2) The culture device does not require traditional aeration, stirring and other power conditions and complex equipment operation. While maintaining the environment required for the growth of Spirulina saltwater, it reduces unnecessary energy consumption and reduces the operating cost of the culture;
(3)反应器主体、反应器顶盖、光源以及盐泽螺旋藻培养架等组件的构造清晰简洁,降低了培养过程的操作难度;反应器主体为长方形箱体结构,尺寸便于操作;(3) The structures of the reactor body, reactor cover, light source, and Spirulina culture rack are clear and concise, which reduces the difficulty of operation during the culture process; the reactor body is a rectangular box structure with a size that is easy to operate;
(4)盐泽螺旋藻培养架可根据实际需要调整培养架的层数,适应不同规模的生产需求,也便于在不同场合下进行运输和安装。(4) The number of layers of the culture rack can be adjusted according to actual needs to meet the production needs of different scales, and it is also convenient for transportation and installation in different occasions.
(5)本培养装置的多层结构设计在垂直方向上充分利用了空间,有效减少占地面积,可在有限的空间内进行规模化生产。(5) The multi-layer structure design of the culture device fully utilizes the space in the vertical direction, effectively reducing the floor space, and can be used for large-scale production within a limited space.
附图说明BRIEF DESCRIPTION OF THE DRAWINGS
构成本发明的一部分的说明书附图用来提供对本发明的进一步理解,本发明的示意性实施例及其说明用于解释本发明,并不构成对本发明的不当限定。The accompanying drawings in the specification, which constitute a part of the present invention, are used to provide a further understanding of the present invention. The exemplary embodiments of the present invention and their descriptions are used to explain the present invention and do not constitute improper limitations on the present invention.
图1为本发明实施例的反应器主体和顶盖的结构示意图;FIG1 is a schematic structural diagram of a reactor body and a top cover according to an embodiment of the present invention;
图2为本发明实施例的反应器主体上方照明单元的结构示意图;FIG2 is a schematic structural diagram of a lighting unit above a reactor body according to an embodiment of the present invention;
图3为本发明实施例的盐泽螺旋藻培养装置的整体结构示意图;FIG3 is a schematic diagram of the overall structure of the Spirulina culturing device of the present invention;
图4为本发明实施例的盐泽螺旋藻培养液的深度优化对比图;FIG4 is a comparison diagram of depth optimization of the culture solution of Spirulina salizawa according to an embodiment of the present invention;
图5为本发明实施例的盐泽螺旋藻培养装置的横截面积优化对比图。FIG. 5 is a comparison diagram of cross-sectional area optimization of the Spirulina salizawa cultivation device according to an embodiment of the present invention.
图中:1、反应器主体;2、反应器顶盖;3、通孔;4、光源;5、固定器;6、连接线;7、培养架;8、光照控制器。In the figure: 1. Reactor body; 2. Reactor top cover; 3. Through hole; 4. Light source; 5. Fixer; 6. Connecting wire; 7. Culture rack; 8. Light controller.
具体实施方式DETAILED DESCRIPTION
应该指出,以下详细说明都是例示性的,旨在对本发明提供进一步的说明。除非另有指明,本发明使用的所有技术和科学术语具有与本发明所属技术领域的普通技术人员通常理解的相同含义。It should be noted that the following detailed descriptions are illustrative and intended to provide further explanation of the present invention. Unless otherwise specified, all technical and scientific terms used in the present invention have the same meanings as those commonly understood by those skilled in the art to which the present invention belongs.
实施例Example
一种盐泽螺旋藻的培养装置,具体如下:A culture device for Spirulina salina, specifically as follows:
如图1-3所示,包括反应器主体1、反应器顶盖2、盐泽螺旋藻培养架7;As shown in FIG1-3 , it includes a reactor body 1, a reactor top cover 2, and a salt-salt Spirulina culture rack 7;
反应器主体1采取箱型结构,反应器顶盖2覆盖于反应器主体1上方,以避免环境污染;The reactor body 1 adopts a box-type structure, and the reactor top cover 2 covers the reactor body 1 to avoid environmental pollution;
反应器顶盖2设有通孔3,同一开口用于加料和气体交换;The reactor top cover 2 is provided with a through hole 3, and the same opening is used for feeding and gas exchange;
螺旋藻培养架7包括多层结构,空间顶部嵌有光源4,底部置有反应器主体1;The spirulina culture rack 7 comprises a multi-layer structure, a light source 4 is embedded in the top of the space, and a reactor body 1 is placed at the bottom;
光源4通过固定器5固定在螺旋藻培养架7每一空间上方,不同光源通过连接线6进行串联,光照控制器8控制光源4;The light source 4 is fixed above each space of the spirulina culture rack 7 by a fixture 5, and different light sources are connected in series by connecting wires 6, and a light controller 8 controls the light source 4;
反应器主体1材料为塑料材质,顶盖为透明薄膜,开有6个通孔;反应器主体1长度为35-95厘米,宽度为25-45厘米,高度为2-10厘米;固定顶部光源的固定器5材质为不锈钢;螺旋藻培养架材料为碳钢,可根据需要将盐泽螺旋藻培养架每一层与光源、反应器主体、反应器顶盖进行组装。The reactor body 1 is made of plastic, and the top cover is a transparent film with 6 through holes; the reactor body 1 is 35-95 cm long, 25-45 cm wide, and 2-10 cm high; the fixture 5 for fixing the top light source is made of stainless steel; the spirulina culture rack is made of carbon steel, and each layer of the salt spirulina culture rack can be assembled with the light source, the reactor body, and the reactor top cover as needed.
使用反应器时,反应器主体1置于螺旋藻培养架7上,加入微藻接种液和培养液,将反应器顶盖2覆盖在反应器主体1上。通过光照控制器8调节光源4设置合适的光照方案和参数,开始微藻培养过程。When the reactor is used, the reactor body 1 is placed on the spirulina culture rack 7, microalgae inoculum and culture solution are added, and the reactor cover 2 is covered on the reactor body 1. The light source 4 is adjusted by the light controller 8 to set a suitable light scheme and parameters to start the microalgae culture process.
对反应器的培养参数进行优化:Optimize the culture parameters of the reactor:
盐泽螺旋藻(Spirulina subsalsa)初始生物质浓度保持在0.1g/L左右,光照为3000lux,培养基为海水添加1‰的味精废水,第三天进行初次收获,补充2‰味精废水后第六天进行再次收获。其中,味精废水和海水使用前分别采用6层纱布和0.45微米滤膜进行过滤,味精废水的总氮、总磷、氨氮为55.26,3.53,47.51g/L,海水的盐度为2.36%;The initial biomass concentration of Spirulina subsalsa was maintained at about 0.1g/L, the light intensity was 3000lux, the culture medium was seawater with 1‰ of MSG wastewater, the first harvest was carried out on the third day, and the second harvest was carried out on the sixth day after adding 2‰ of MSG wastewater. Among them, the MSG wastewater and seawater were filtered with 6 layers of gauze and 0.45 micron filter membrane respectively before use. The total nitrogen, total phosphorus and ammonia nitrogen of the MSG wastewater were 55.26, 3.53 and 47.51g/L, and the salinity of the seawater was 2.36%;
螺旋藻培养液的三种不同深度:2.25cm,4.5cm,9cm;Three different depths of Spirulina culture medium: 2.25cm, 4.5cm, and 9cm;
三种不同的横截面:长×宽为38×26=988cm2;长×宽为71×28=1988cm2;长×宽为93×43=3999cm2。Three different cross sections: length×width is 38×26=988 cm 2 ; length×width is 71×28=1988 cm 2 ; length×width is 93×43=3999 cm 2 .
选出最合适的横截面积后,得出合适反应器主体尺寸。依据公式计算生物质浓度:After selecting the most suitable cross-sectional area, the appropriate reactor body size is obtained. The biomass concentration is calculated according to the formula:
式中:DM3为第三天收获藻粉的重量;DM6为第三天收获藻粉的重量;V为培养体积。Wherein: DM 3 is the weight of algal powder harvested on the third day; DM 6 is the weight of algal powder harvested on the third day; V is the culture volume.
反应器内培养液的最佳深度为4.5cm时盐泽螺旋藻生长最佳,生物质浓度可达0.84g/L;培养液的深度为2.25cm时,盐泽螺旋藻的浓度可达0.75g/L;培养液的深度为9cm时,盐泽螺旋藻的浓度可达0.52g/L,如图4所示。反应器主体横截面积为988cm2和1988cm2时盐泽螺旋藻生物质浓度可达0.83g/L和0.82g/L;反应器主体横截面积为3999cm2时,盐泽螺旋藻生物质浓度可达0.72g/L,如图5所示。因此,盐泽螺旋藻培养反应器内培养液的合适深度和面积分别为4.5cm和1988cm2。When the optimal depth of the culture solution in the reactor is 4.5 cm, the growth of Spirulina is the best, and the biomass concentration can reach 0.84 g/L; when the depth of the culture solution is 2.25 cm, the concentration of Spirulina can reach 0.75 g/L; when the depth of the culture solution is 9 cm, the concentration of Spirulina can reach 0.52 g/L, as shown in Figure 4. When the cross-sectional area of the reactor body is 988 cm2 and 1988 cm2 , the biomass concentration of Spirulina can reach 0.83 g/L and 0.82 g/L; when the cross-sectional area of the reactor body is 3999 cm2 , the biomass concentration of Spirulina can reach 0.72 g/L, as shown in Figure 5. Therefore, the appropriate depth and area of the culture solution in the reactor for cultivating Spirulina are 4.5 cm and 1988 cm2 , respectively.
以上所述仅为本发明的优选实施例而已,并不用于限制本发明,对于本领域的技术人员来说,本发明可以有各种更改和变化。凡在本发明的精神和原则之内,所作的任何修改、等同替换、改进等,均应包含在本发明的保护范围之内。The above description is only a preferred embodiment of the present invention and is not intended to limit the present invention. For those skilled in the art, the present invention may have various modifications and variations. Any modification, equivalent replacement, improvement, etc. made within the spirit and principle of the present invention shall be included in the protection scope of the present invention.
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