CN116179303A - Culture device and method based on gas preconfiguration and circulation supply - Google Patents
Culture device and method based on gas preconfiguration and circulation supply Download PDFInfo
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Abstract
Description
技术领域technical field
本发明涉及微生物培育技术领域,尤其涉及基于气体预配和循环供给的培养装置及方法。The invention relates to the technical field of microorganism cultivation, in particular to a cultivation device and method based on gas preconfiguration and circulation supply.
背景技术Background technique
秸秆等农业大宗废弃物的资源化利用关系到农业、生态环境和社会经济的可持续发展。生物转化与合成技术是实现这些废弃物资源化利用的有效手段,但目前生物转化仅关注终端产品,对产生的CO2等尾气尚未加以充分利用,而这部分CO2可能占到整个生物质碳含量的50%左右。将这一半的碳充分利用,对实现废弃物高值转化和碳减排具有重要的意义。The resource utilization of agricultural bulk waste such as straw is related to the sustainable development of agriculture, ecological environment and social economy. Biotransformation and synthesis technology is an effective means to realize the resource utilization of these wastes, but at present, biotransformation only focuses on the end products, and the exhaust gas such as CO2 has not been fully utilized, and this part of CO2 may account for the entire biomass carbon content. About 50%. Making full use of this half of the carbon is of great significance for realizing high-value waste conversion and carbon emission reduction.
现有的CO2发酵尾气循环培养装置重点聚焦于发酵产物CO2尾气的处理,将CO2尾气经过简单的过滤后直接用于循环培养,这样的方式较为简单有效,但存在以下问题:The existing CO2 fermentation tail gas circulation culture device focuses on the treatment of the fermentation product CO2 tail gas. The CO2 tail gas is directly used for circulation culture after simple filtration. This method is relatively simple and effective, but there are the following problems:
1、供气精准度差;通气时会由于液位压力导致各种配方气体不按照设定流量进入发酵系统,导致供气不稳定,通气量不准确;尤其是多罐并联时,由于曝气头和液位差问题经常导致不同发酵罐之间曝气量差异很大,甚至发生串气问题。1. The accuracy of gas supply is poor; when ventilating, various formula gases will not enter the fermentation system according to the set flow rate due to liquid level pressure, resulting in unstable gas supply and inaccurate ventilation; especially when multiple tanks are connected in parallel, due to aeration Head and liquid level difference problems often lead to large differences in aeration between different fermenters, and even cross-gas problems.
2、适用范围较窄;主要适用于发酵尾气和培养气体相同的生物转化过程,主要适用于微藻类的生物循环培养,当将其应用到需要混合气体培养的场景中时,由于其气体循环只包含CO2等单一尾气,因此需要采用额外的供气设施设备;2. The scope of application is narrow; it is mainly suitable for the biotransformation process of the same fermentation tail gas and culture gas, and is mainly suitable for the biological cycle culture of microalgae. When it is applied to the scene that requires mixed gas culture, because its gas cycle only Contains single exhaust gas such as CO2, so additional gas supply facilities and equipment are required;
3、需要人工值守;在系统工作的过程中,需要技术人员现场值守,根据培养过程调整各供料与气体循环的具体参数,以保证培养过程的顺利进行;3. Manual on-duty is required; during the working process of the system, technical personnel are required to be on-site to adjust the specific parameters of each feeding and gas circulation according to the cultivation process to ensure the smooth progress of the cultivation process;
4、尾气不适于直接用于循环培养;发酵尾气的浓度一般偏高,且其混合其他的各组分比例并不固定,在循环进行培养时无法保证气体中各组分的比例是适宜培养的,尤其当尾气中某一气体浓度偏高时(如CO2),可能会对培养过程造成较为不利的影响。4. The tail gas is not suitable for direct use in circulation culture; the concentration of fermentation tail gas is generally high, and the proportion of other components mixed with it is not fixed, so it cannot be guaranteed that the proportion of each component in the gas is suitable for culture in circulation culture , especially when the concentration of a certain gas in the tail gas is too high (such as CO2), it may cause relatively adverse effects on the cultivation process.
发明内容Contents of the invention
为了解决上述技术问题,本发明提供了适用于多种应用场景的、基于气体预配和循环供给的自动培养装置及方法。In order to solve the above-mentioned technical problems, the present invention provides an automatic culture device and method based on gas preconfiguration and cyclic supply, which are applicable to various application scenarios.
为了实现上述技术目的,本发明所提供的技术方案包括:In order to realize the above technical purpose, the technical solutions provided by the present invention include:
基于气体预配和循环供给的培养装置,包括:A culture device based on gas preconfiguration and circulation supply, including:
通过第一管路连通的若干培养瓶,所述第一管路上还连通有进出液系统;A number of culture bottles communicated through the first pipeline, and the first pipeline is also connected with an inlet and outlet liquid system;
三通阀,所述三通阀分别连通预装气罐、通过气体计量泵连通气源,还通过第二管路连通培养瓶,所述第二管路上设置有气体浓度传感器;A three-way valve, the three-way valve is connected to the pre-installed gas tank, the gas source through the gas metering pump, and the culture bottle through the second pipeline, and the gas concentration sensor is arranged on the second pipeline;
预装气罐还通过第三管路与培养瓶连通,所述第三管路上设置有循环泵;The pre-installed gas tank is also communicated with the culture bottle through a third pipeline, and a circulating pump is arranged on the third pipeline;
培养瓶连接有检测瓶内液体浊度的浊度传感器,和检测瓶内液体高度的第一液位传感器;The culture bottle is connected with a turbidity sensor for detecting the turbidity of the liquid in the bottle, and a first liquid level sensor for detecting the height of the liquid in the bottle;
预装气罐连接有检测罐内气体压力的压力传感器,和检测罐内液体高度的第二液位传感器;The pre-installed gas tank is connected with a pressure sensor to detect the gas pressure in the tank, and a second liquid level sensor to detect the liquid height in the tank;
所述预装气罐还设置有第一出液端和排气端;The pre-installed gas tank is also provided with a first liquid outlet end and an exhaust end;
第一电磁阀,用于控制第二管路和第三管路分别与各培养瓶的连通关系;The first electromagnetic valve is used to control the communication relationship between the second pipeline and the third pipeline and each culture bottle;
第二电磁阀,用于控制预装气罐与第三管路的连通关系;The second solenoid valve is used to control the communication relationship between the pre-installed gas tank and the third pipeline;
其中,所述第二管路连通培养瓶的一端位于所述培养液面以上;所述第一管路和第三管路连通培养瓶的一端位于所述培养液面以下。Wherein, one end of the second pipeline connected to the culture bottle is located above the culture liquid level; one end of the first pipeline and the third pipeline connected to the culture bottle is located below the culture liquid level.
在一些较优的实施例中,所述进出液系统包括分别并行且与所述第一管路连通的进液端和第二出液端;所述进液端和第二出液端分别设置有电磁阀和液体计量泵。In some preferred embodiments, the liquid inlet and outlet system includes a liquid inlet and a second liquid outlet in parallel and communicated with the first pipeline; the liquid inlet and the second liquid outlet are respectively set There are solenoid valves and liquid metering pumps.
在一些较优的实施例中,所述第三管路伸入培养瓶的一端设置有曝气头。In some preferred embodiments, an aeration head is provided at one end of the third pipeline extending into the culture bottle.
在一些较优的实施例中,所述培养瓶前、第一电磁阀后的第三管路上设置有可调阻尼器。In some preferred embodiments, an adjustable damper is provided on the third pipeline in front of the culture bottle and behind the first electromagnetic valve.
本发明还提供过了一种基于气体预配和循环供给的培养方法,包括:The present invention also provides a cultivation method based on gas preconfiguration and circulation supply, including:
S1、通过进出液系统分别向若干培养瓶中加入定量的培养液;S1. Add quantitative culture solution to several culture bottles through the liquid inlet and outlet system;
S2、三通阀导通预装气罐和气源,通过气源向预装气罐中加定量的原料气;S2. The three-way valve conducts the pre-installed gas tank and the gas source, and adds a certain amount of raw material gas to the pre-installed gas tank through the gas source;
S3、三通阀导通预装气罐和第二管路,打开第一电磁阀和第二电磁阀,启动循环泵,使气体按预装气罐、第三管路、培养瓶、第二管路和三通阀的顺序循环流动;S3. The three-way valve conducts the pre-installed gas tank and the second pipeline, opens the first solenoid valve and the second solenoid valve, starts the circulation pump, and makes the gas flow through the pre-installed gas tank, the third pipeline, the culture bottle, and the second pipeline. Sequential circulation of pipelines and three-way valves;
S4、当气体浓度传感器的检测值达到预定值时,关闭循环泵,打开排气端并收集排出气体,当罐内压力恢复大气压时关闭排气端,重复执行步骤S2-S4。S4. When the detection value of the gas concentration sensor reaches the predetermined value, turn off the circulation pump, open the exhaust end and collect the exhaust gas, close the exhaust end when the pressure in the tank returns to atmospheric pressure, and repeat steps S2-S4.
在一些较优的实施例中,还包括步骤:In some preferred embodiments, it also includes the steps of:
当浊度传感器的检测值达到预定值时,控制第一电磁阀保持导通第三管路与培养瓶,关闭第二管路与培养瓶的导通;通过进出液系统导出定量的旧培养液,并补充相同量的新培养液;补充完成后,控制第一电磁阀保持导通第三管路与培养瓶,打开第二管路与培养瓶的导通。When the detection value of the turbidity sensor reaches the predetermined value, control the first electromagnetic valve to keep the third pipeline and the culture bottle connected, and close the conduction between the second pipeline and the culture bottle; the quantitative old culture solution is exported through the liquid inlet and outlet system , and supplement the same amount of new culture solution; after the supplement is completed, control the first solenoid valve to keep the third pipeline connected to the culture bottle, and open the second pipeline to the culture bottle.
在一些较优的实施例中,还包括步骤:In some preferred embodiments, it also includes the steps of:
当第二液位传感器监测到预装气罐中液面高度达到预设时,通过第一出液端导出罐内液体;当压力传感器监测到预装气罐中气体压力达到预设时,打开排气端以降低罐内压力。When the second liquid level sensor detects that the liquid level in the pre-installed gas tank reaches the preset height, the liquid in the tank is led out through the first liquid outlet; when the pressure sensor detects that the gas pressure in the pre-installed gas tank reaches the preset value, it opens Vent to reduce tank pressure.
有益效果Beneficial effect
1、本发明通过预装气罐和循环管路对气体进行批次化处理,可实现不间断气体配制和供给,并有效提高原料气的利用率;2、避免因液位压力导致配方气体不按照设定流量供应的问题,可提高气体在液体中的均匀分布程度,尤其在不能搅拌的条件下有优势;3、通过阻尼器有效平衡各个罐体的进气压力,不显著增加经济成本情况下通过简单手段实现每罐的通气量一致,保障连续稳定作业;4、通过预设各传感器的参数,配合循环管路,可实现无人值守情况下的自动进行气体处理、气体收集、培养物收集和培养液添加等功能,节约人工成本和时间成本,提高培养效率;5、采用模块化组件,可根据实际需要自由组合,以实现定制化的功能和处理量。1. The present invention conducts batch processing of gas through pre-installed gas tanks and circulation pipelines, which can realize uninterrupted gas preparation and supply, and effectively improve the utilization rate of raw gas; According to the problem of the set flow supply, the uniform distribution of the gas in the liquid can be improved, especially under the condition that it cannot be stirred; 3. The damper can effectively balance the inlet pressure of each tank without significantly increasing the economic cost. Through simple means, the ventilation volume of each tank is consistent, ensuring continuous and stable operation; 4. By presetting the parameters of each sensor and coordinating with the circulation pipeline, automatic gas processing, gas collection, and culture can be realized under unattended conditions. Functions such as collection and addition of culture medium save labor costs and time costs and improve culture efficiency; 5. Modular components are used, which can be freely combined according to actual needs to achieve customized functions and processing capacity.
附图说明Description of drawings
图1为本发明一种较优实施例中的基于气体预配和循环供给的培养装置结构示意图;Fig. 1 is a schematic structural diagram of a culture device based on gas pre-allocation and circulation supply in a preferred embodiment of the present invention;
图2为本发明另一种较优实施例中的基于气体预配和循环供给的培养方法流程示意图;Fig. 2 is a schematic flow chart of a culture method based on gas pre-allocation and cyclic supply in another preferred embodiment of the present invention;
图中:1、培养瓶;2、进出液系统;3、三通阀;4、预装气罐;5、气源;6、气体计量泵;7、第二管路;8、气体浓度传感器;9、第三管路;10、循环泵;11、浊度传感器;12、第一管路;13、第一液位传感器;14、压力传感器;15、第二液位传感器;16、第一出液端;17、排气端;18、第一电磁阀;19、第二电磁阀;20、安全阀;21、阻尼器;22、液体计量泵;101、曝气头;201、进液端;202、第二出液端;In the figure: 1. culture bottle; 2. liquid inlet and outlet system; 3. three-way valve; 4. pre-installed gas tank; 5. gas source; 6. gas metering pump; 7. second pipeline; 8. gas concentration sensor ;9, the third pipeline; 10, circulation pump; 11, turbidity sensor; 12, the first pipeline; 13, the first liquid level sensor; 14, pressure sensor; 15, the second liquid level sensor; 16, the first 1. Outlet end; 17. Exhaust end; 18. First solenoid valve; 19. Second solenoid valve; 20. Safety valve; 21. Damper; 22. Liquid metering pump; 101. Aerator head; 201. Inlet Liquid end; 202, the second liquid outlet;
具体实施方式Detailed ways
为了使本发明的目的、技术方案和优点更加清楚,下面结合附图对本发明作进一步阐述。在本发明的描述中,需要理解的是,术语“上”、“下”、“前”、“后”、“左”、“右”、“顶”、“底”、“内”、“外”等指示的方位或位置关系为基于附图所示的方位或位置关系,仅是为了便于描述本发明和简化描述,而不是指示或暗示所指的装置或元件必须具有特定的方位、以特定的方位构造和操作,因此不能理解为对本发明的限制。In order to make the purpose, technical solution and advantages of the present invention clearer, the present invention will be further elaborated below in conjunction with the accompanying drawings. In describing the present invention, it should be understood that the terms "upper", "lower", "front", "rear", "left", "right", "top", "bottom", "inner", " The orientation or positional relationship indicated by "outside", etc. is based on the orientation or positional relationship shown in the drawings, and is only for the convenience of describing the present invention and simplifying the description, rather than indicating or implying that the referred device or element must have a specific orientation, so as to Specific orientation configurations and operations, therefore, are not to be construed as limitations on the invention.
如图1所示,本实施例提供了一种基于气体预配和循环供给的培养装置,包括:As shown in Figure 1, this embodiment provides a culture device based on gas preconfiguration and circulation supply, including:
通过第一管路12连通的若干培养瓶1,所述第一管路12上还连通有进出液系统2;其中,本领域技术人员可以根据实际的培养量需要合理设定具体的培养瓶1数量,还可以根据实际的培养条件用耐压透明材料制作或采用金属罐体,可安装于具有恒温,光照和搅拌等功能的基座上,可增加对酸碱度、离子浓度等指标进行监测和控制的其他配套装置及设备。所述进出液系统2是为了补充和\或收集培养瓶1中的培养液,其具体实现方式可以由本领域技术人员根据常见的补液出液方式设置。在一些较优的实施例中,给出了一种分路实现进出液的方式,具体包括:A number of culture bottles 1 communicated through the first pipeline 12, and the first pipeline 12 is also connected with the liquid inlet and outlet system 2; wherein, those skilled in the art can reasonably set specific culture bottles 1 according to the needs of the actual culture volume The quantity can also be made of pressure-resistant transparent materials or metal tanks according to the actual culture conditions. It can be installed on a base with functions such as constant temperature, light and stirring, and can increase the monitoring and control of pH, ion concentration and other indicators. other ancillary devices and equipment. The liquid inlet and outlet system 2 is for supplementing and/or collecting the culture fluid in the culture bottle 1, and its specific implementation can be set by those skilled in the art according to the common fluid replenishment and fluid outlet methods. In some preferred embodiments, a way to achieve liquid inlet and outlet by shunting is provided, including:
所述进出液系统2包括分别并行且与所述第一管路12连通的进液端201和第二出液端202;所述进液端201和第二出液端202分别设置有电磁阀和液体计量泵22。The liquid inlet and outlet system 2 includes a
三通阀3,所述三通阀3分别连通预装气罐4、通过气体计量泵6连通气源5,还通过第二管路7连通培养瓶1,所述第二管路7上设置有气体浓度传感器8;Three-way valve 3, the three-way valve 3 communicates with the pre-installed gas tank 4, the gas source 5 through the gas metering pump 6, and the culture bottle 1 through the second pipeline 7, and the second pipeline 7 is provided with There is a
预装气罐4还通过第三管路9与培养瓶1连通,所述第三管路9上设置有循环泵10;The pre-installed gas tank 4 is also communicated with the culture bottle 1 through the
培养瓶1连接有检测瓶内液体浊度的浊度传感器11,和检测瓶内液体高度的第一液位传感器13;The culture bottle 1 is connected with a
预装气罐4连接有检测罐内气体压力的压力传感器14,和检测罐内液体高度的第二液位传感器15;The prepacked gas tank 4 is connected with a
所述预装气罐4还设置有第一出液端16和排气端17;其中,所述第一出液端16可以通过电磁阀控制出液过程和出液量;所述排气端17包括电磁阀和与电磁阀导通的气体计量泵6,用于控制预装气罐4的排气过程和排气体积。The pre-installed gas tank 4 is also provided with a first liquid outlet end 16 and an exhaust end 17; wherein, the first liquid outlet end 16 can control the liquid outlet process and the amount of liquid outlet through a solenoid valve; the exhaust end 17 includes a solenoid valve and a gas metering pump 6 connected with the solenoid valve, which is used to control the exhaust process and exhaust volume of the pre-installed gas tank 4 .
第一电磁阀18,用于控制第二管路7和第三管路9分别与各培养瓶1的连通关系;The first
第二电磁阀19,用于控制预装气罐4与第三管路9的连通关系;The second
其中,所述第二管路7连通培养瓶1的一端位于所述培养液面以上;所述第一管路12和第三管路9连通培养瓶1的一端位于所述培养液面以下。在一些较优的实施例中,为了增加通入培养液的气体曝气量,考虑在所述第三管路9伸入培养瓶1的一端设置曝气头101。Wherein, one end of the second pipeline 7 connected to the culture bottle 1 is located above the culture liquid level; the ends of the first pipeline 12 and the
在另一些较优的实施例中,为了确保每个培养瓶1的进气量一致,可以在培养瓶1前、第一电磁阀18后的第三管路9上设置有可调阻尼器21。In other preferred embodiments, in order to ensure that the air intake of each culture bottle 1 is consistent, an
应当理解的是,为了实现对上述各类传感器的数据进行采集和处理,并根据相关参数设置各电磁阀和泵类装置的启闭,本发明中显然还应当有能够实现上述功能的控制器,该控制器与各类传感器、电磁阀和泵类装置电连接,以实现对整个培养过程的控制。It should be understood that, in order to collect and process the data of the above-mentioned various sensors, and set the opening and closing of each electromagnetic valve and pump device according to relevant parameters, the present invention should obviously also have a controller capable of realizing the above-mentioned functions. The controller is electrically connected with various sensors, electromagnetic valves and pump devices to realize the control of the entire cultivation process.
下面就本实施例的工作过程及原理作如下描述:The working process and principle of the present embodiment are described as follows:
1、初始状态设定:根据各培养瓶1的体积计算所需加入的培养液体积,并将第一液位传感器13的液位检测值设定为对应参数;根据整个系统的气体可占用空间计算需要加入预装气罐4的原料气体积,据此设定气体计量泵6的气体流量参数和预装气罐4内的压力传感器14参数;根据现场的实际需要设定取料的液体浊度和取料体积,根据培养进程的演化设定触发补气的气体浓度下限;根据预装气罐4体积设定第二液位传感器15的液位检测值,以检查在预装气罐4中冷凝的液体体积,当冷凝液体体积达到第二液位传感器15的液位检测值时,则需要将预装气罐4中的液体排出。1. Initial state setting: Calculate the volume of culture solution to be added according to the volume of each culture bottle 1, and set the liquid level detection value of the first
2、培养液的加入:三通阀3导通第二管路7和预装气罐4,第二电磁阀19导通,第一电磁阀18导通第二管路7和培养瓶1、关闭第三管路9和培养瓶1,打开第一出液端16,通过进出液系统2向各培养瓶1加入预设的培养液体积;加液完成后,关闭第一出液端16。2. The addition of the culture solution: the three-way valve 3 is connected to the second pipeline 7 and the pre-installed gas tank 4, the
3、气体管路的压力平衡:打开预装气罐4上的排气端17,平衡罐内外压力,并将排出的气体收集起来送到下一级处理装置或存储装置;平衡完毕后关闭预装气罐4上的排气端17。3. Pressure balance of the gas pipeline: open the exhaust port 17 on the pre-installed gas tank 4, balance the pressure inside and outside the tank, and collect the discharged gas and send it to the next-level processing device or storage device; close the pre-installed gas tank after the balance is completed. The exhaust port 17 on the gas tank 4.
4、原料气的加入:关闭第一电磁阀18、第二电磁阀19和循环泵10,三通阀3导通气源5和预装气罐4,气体计量泵6向预装气罐4中加入预设的原料气体积;4. Adding raw material gas: close the
5、气体循环培养:加气完成后,三通阀3导通预装气罐4和第二管路7,打开第二电磁阀19,打开第一电磁阀18以分别导通第二管路7和第三管路9与各培养瓶1,启动循环泵10,此时,气体将在培养瓶1和预装气罐4间循环。5. Gas cycle cultivation: After gas filling is completed, the three-way valve 3 leads to the pre-installed gas tank 4 and the second pipeline 7, opens the
6、原料气的补充:当气体浓度传感器8检测到气体浓度低于预设值时,重复执行3-5;6. Supplementation of raw material gas: when the
7、培养液的提取:当浊度传感器11检测到培养液浊度达到预设值时,第一电磁阀18关闭第二管路7与各培养瓶1的导通,利用进出液系统2抽取预设体积的旧培养液,并补充相应体积的新培养液,重新加液完成后,第一电磁阀18打开第二管路7与各培养瓶1的导通。7. Extraction of the culture solution: when the
8、冷凝水的排放:根据预装气罐4体积在第一液位传感器13设定适宜的冷凝水液面高度,当预装气罐4内的冷凝水达到该预设高度时,打开第一出液端16,排放罐内的冷凝水,以避免冷凝液在罐内储蓄过多。8. Drainage of condensed water: according to the volume of the pre-installed gas tank 4, set the appropriate height of the condensed water level in the first
9、预装气罐4压力保护:当预装气罐4内的压力传感器14检测到罐内压力大于预设值,打开预装气罐4上的排气端17,平衡罐内外压力,并将排出的气体收集起来送到下一级处理装置或存储装置;平衡完毕后关闭预装气罐4上的排气端17。在一些较优的实施例中,为了防止压力传感器14失效引起超压,所述预装气罐4上还可以设置有安全阀20。9. Pressure protection of pre-installed gas tank 4: When the
10、配方气体的预混配置:当培养过程需要多种组分的原料气供应时,关闭第一电磁阀18、第二电磁阀19和循环泵10,三通阀3导通气源5和预装气罐4,气体计量泵6向预装气罐4中分别加入各预设体积的不同种类原料气,实现配方气体的精确配置。10. Premix configuration of formula gas: when the cultivation process requires the supply of raw material gas of various components, close the
实施例2Example 2
本实施例是在上述实施例1的基础上展开的,如图2所示,本实施例给出了一种基于气体预配和循环供给的培养方法,包括:This embodiment is developed on the basis of the above-mentioned embodiment 1, as shown in Figure 2, this embodiment provides a cultivation method based on gas pre-allocation and circulating supply, including:
S1、通过进出液系统2分别向若干培养瓶1中加入定量的培养液;S1. Add quantitative culture solution to several culture bottles 1 through the liquid inlet and outlet system 2;
S2、三通阀3导通预装气罐4和气源5,通过气源5向预装气罐4中加定量的原料气;S2. The three-way valve 3 connects the pre-installed gas tank 4 and the gas source 5, and adds a certain amount of raw material gas to the pre-installed gas tank 4 through the gas source 5;
S3、三通阀3导通预装气罐4和第二管路7,打开第一电磁阀18和第二电磁阀19,启动循环泵10,使气体按预装气罐4、第三管路9、培养瓶1、第二管路7和三通阀3的顺序循环流动;S3, the three-way valve 3 conducts the pre-installed gas tank 4 and the second pipeline 7, opens the
S4、当气体浓度传感器8的检测值达到预定值时,关闭循环泵10,打开排气端17并收集排出气体,当罐内压力恢复大气压时关闭排气端17,重复执行步骤S2-S4。S4. When the detection value of the
在另一些较优的实施例中,还给出了一种自动控制旧培养液与新培养液导出导入的具体方法,包括步骤:In other preferred embodiments, a specific method for automatically controlling the import and export of old culture fluid and new culture fluid is also provided, including steps:
当浊度传感器11的检测值达到预定值时,控制第一电磁阀18保持导通第三管路9与培养瓶1,关闭第二管路7与培养瓶1的导通;通过进出液系统2导出定量的旧培养液,并补充相同量的新培养液;补充完成后,控制第一电磁阀18保持导通第三管路9与培养瓶1,打开第二管路7与培养瓶1的导通。When the detection value of the
在另一些较优的实施例中,给出了一种控制预装气罐4内液体和气体体积的方法,具体包括步骤:In other preferred embodiments, a method for controlling the volume of liquid and gas in the pre-packed gas tank 4 is provided, specifically including steps:
当第二液位传感器15监测到预装气罐4中液面高度达到预设时,通过第一出液端16导出罐内液体;当压力传感器14监测到预装气罐4中气体压力达到预设时,打开排气端17以降低罐内压力。When the second
实施例3Example 3
本实施例是在上述实施例1和2的基础上展开的,本发明所提供的基于气体预配和循环供给的培养方法及装置,适用于对一种或多种气体进行浓度和比例的分配,应用于细菌、酵母、食用菌、藻类等生物培养以及需要混合气体配制的化学反应。下面给出两个具体的应用场景示例:This embodiment is developed on the basis of the above-mentioned embodiments 1 and 2. The cultivation method and device based on gas pre-allocation and circulation supply provided by the present invention are suitable for the distribution of concentration and ratio of one or more gases , used in the biological culture of bacteria, yeast, edible fungus, algae and other chemical reactions that require mixed gas preparation. Two examples of specific application scenarios are given below:
应用场景一Application Scenario 1
可利用本发明所提供的于气体预配和循环供给的培养方法及装置,配制不同浓度的单一气体,用于微藻培养。将高纯二氧化碳(CO2)气体准确配制成0.04%、4%和40%不同浓度,实现一种浓度在设定的时间周期内开启或关闭,用于微藻A的培养;或者3种浓度按照设定要求,在设定的时间周期内开启或关闭,依次对微藻培养液进行充气培养,最终实现CO2气体的循环供给、高效利用和微藻的高效生长。The cultivation method and device for gas preconfiguration and circulation supply provided by the present invention can be used to prepare single gas with different concentrations for microalgae cultivation. Accurately prepare high-purity carbon dioxide (CO2) gas into different concentrations of 0.04%, 4% and 40%, so that one concentration can be turned on or off within a set time period for the cultivation of microalgae A; Set the requirements, turn on or off within the set time period, and carry out aerated culture of the microalgae culture solution in turn, and finally realize the cyclic supply of CO2 gas, efficient utilization and efficient growth of microalgae.
应用场景二Application Scenario 2
可利用本发明所提供的于气体预配和循环供给的培养方法及装置,将多种气体按比例混合,用于微生物培养。将高纯二氧化碳(CO2)气体和氢气(H2)按照需求比例混合,用于细菌B的培养。实现了气体的不间断配制和循环供给。The cultivation method and device for gas preconfiguration and circulation supply provided by the present invention can be used to mix various gases in proportion for microbial cultivation. Mix high-purity carbon dioxide (CO2) gas and hydrogen (H2) according to the required ratio for the cultivation of bacteria B. Realize the uninterrupted preparation and circulation supply of gas.
以上显示和描述了本发明的基本原理、主要特征和本发明的优点。本行业的技术人员应该了解,本发明不受上述实施例的限制,上述实施例和说明书中描述的只是说明本发明的原理,在不脱离本发明精神和范围的前提下,本发明还会有各种变化和改进,这些变化和改进都落入要求保护的本发明范围内。本发明要求保护范围由所附的权利要求书及其等效物界定。The basic principles, main features and advantages of the present invention have been shown and described above. Those skilled in the industry should understand that the present invention is not limited by the above-mentioned embodiments. What are described in the above-mentioned embodiments and the description only illustrate the principle of the present invention. Without departing from the spirit and scope of the present invention, the present invention will also have Variations and improvements are possible, which fall within the scope of the claimed invention. The protection scope of the present invention is defined by the appended claims and their equivalents.
Claims (7)
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Citations (10)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2008040365A1 (en) * | 2006-10-06 | 2008-04-10 | Tallinn University Of Technology | Method and system for fed-batch cultivation of hydrogen-oxidizing bacteria |
| CN201065407Y (en) * | 2007-06-14 | 2008-05-28 | 华中科技大学同济医学院附属同济医院 | In vitro cell open pressure program-controlled culture device |
| CN103045470A (en) * | 2011-10-14 | 2013-04-17 | 吴俊宗 | Circulation closed microalgae culture production system |
| KR20150006718A (en) * | 2013-07-09 | 2015-01-19 | (주)엔엘피 | Microalgal Cultivation Facility Using Closed Carbon Dioxide Photobioreactor |
| CN105571042A (en) * | 2016-02-26 | 2016-05-11 | 华南理工大学 | Exhaust system for realizing multi-point uniform flow based on linear processing and method thereof |
| CN106907571A (en) * | 2017-02-21 | 2017-06-30 | 重庆川仪分析仪器有限公司 | Airline pressure control system and total carbon-hydrogen analyzer |
| CN112228770A (en) * | 2020-09-20 | 2021-01-15 | 广东韶钢松山股份有限公司 | Automatic drainage device of compressed air tank and use method |
| CN213388602U (en) * | 2020-08-18 | 2021-06-08 | 广西小藻农业科技有限公司 | Little algae culture rack |
| CN214840156U (en) * | 2021-05-11 | 2021-11-23 | 华能(福建漳州)能源有限责任公司 | A compressed air condensate drainage system |
| CN115386488A (en) * | 2022-04-21 | 2022-11-25 | 山东威高瑞生医疗器械有限公司 | A gas supply system for a cell culture box and a method for dynamic control of gas concentration |
-
2022
- 2022-12-29 CN CN202211704245.3A patent/CN116179303A/en active Pending
Patent Citations (10)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2008040365A1 (en) * | 2006-10-06 | 2008-04-10 | Tallinn University Of Technology | Method and system for fed-batch cultivation of hydrogen-oxidizing bacteria |
| CN201065407Y (en) * | 2007-06-14 | 2008-05-28 | 华中科技大学同济医学院附属同济医院 | In vitro cell open pressure program-controlled culture device |
| CN103045470A (en) * | 2011-10-14 | 2013-04-17 | 吴俊宗 | Circulation closed microalgae culture production system |
| KR20150006718A (en) * | 2013-07-09 | 2015-01-19 | (주)엔엘피 | Microalgal Cultivation Facility Using Closed Carbon Dioxide Photobioreactor |
| CN105571042A (en) * | 2016-02-26 | 2016-05-11 | 华南理工大学 | Exhaust system for realizing multi-point uniform flow based on linear processing and method thereof |
| CN106907571A (en) * | 2017-02-21 | 2017-06-30 | 重庆川仪分析仪器有限公司 | Airline pressure control system and total carbon-hydrogen analyzer |
| CN213388602U (en) * | 2020-08-18 | 2021-06-08 | 广西小藻农业科技有限公司 | Little algae culture rack |
| CN112228770A (en) * | 2020-09-20 | 2021-01-15 | 广东韶钢松山股份有限公司 | Automatic drainage device of compressed air tank and use method |
| CN214840156U (en) * | 2021-05-11 | 2021-11-23 | 华能(福建漳州)能源有限责任公司 | A compressed air condensate drainage system |
| CN115386488A (en) * | 2022-04-21 | 2022-11-25 | 山东威高瑞生医疗器械有限公司 | A gas supply system for a cell culture box and a method for dynamic control of gas concentration |
Non-Patent Citations (1)
| Title |
|---|
| 潘轩等: "用于细胞培养实验的定量抽气-充气方法及相配装置", 生物技术通讯, vol. 25, no. 05, 30 September 2015 (2015-09-30), pages 691 - 696 * |
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