CN216274173U - A low-shear air-lift fermenter oxygenation and mixing device - Google Patents
A low-shear air-lift fermenter oxygenation and mixing device Download PDFInfo
- Publication number
- CN216274173U CN216274173U CN202120554944.9U CN202120554944U CN216274173U CN 216274173 U CN216274173 U CN 216274173U CN 202120554944 U CN202120554944 U CN 202120554944U CN 216274173 U CN216274173 U CN 216274173U
- Authority
- CN
- China
- Prior art keywords
- air
- stone
- gas
- airlift
- stones
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Active
Links
- 238000002156 mixing Methods 0.000 title claims abstract description 31
- 238000006213 oxygenation reaction Methods 0.000 title claims description 11
- 239000004575 stone Substances 0.000 claims abstract description 78
- 239000002184 metal Substances 0.000 claims abstract description 29
- 238000000855 fermentation Methods 0.000 claims abstract description 28
- 230000004151 fermentation Effects 0.000 claims abstract description 28
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 claims abstract description 24
- 239000007788 liquid Substances 0.000 claims abstract description 24
- 239000001301 oxygen Substances 0.000 claims abstract description 24
- 229910052760 oxygen Inorganic materials 0.000 claims abstract description 24
- 238000005273 aeration Methods 0.000 claims abstract description 12
- 239000007789 gas Substances 0.000 claims description 33
- 238000007789 sealing Methods 0.000 claims description 11
- 239000000203 mixture Substances 0.000 claims description 4
- 241000251468 Actinopterygii Species 0.000 claims description 2
- 239000004576 sand Substances 0.000 claims description 2
- 238000005245 sintering Methods 0.000 claims description 2
- 238000005276 aerator Methods 0.000 claims 2
- 238000010008 shearing Methods 0.000 claims 1
- 238000005265 energy consumption Methods 0.000 abstract description 5
- 239000000463 material Substances 0.000 abstract description 4
- 241001465754 Metazoa Species 0.000 abstract description 2
- 241000894006 Bacteria Species 0.000 abstract 1
- 244000005700 microbiome Species 0.000 abstract 1
- 210000004027 cell Anatomy 0.000 description 12
- 238000009423 ventilation Methods 0.000 description 6
- 210000004102 animal cell Anatomy 0.000 description 4
- 238000001816 cooling Methods 0.000 description 4
- 230000006872 improvement Effects 0.000 description 3
- 210000001938 protoplast Anatomy 0.000 description 3
- 238000004113 cell culture Methods 0.000 description 2
- 210000002421 cell wall Anatomy 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- 238000011081 inoculation Methods 0.000 description 2
- 230000004048 modification Effects 0.000 description 2
- 238000012986 modification Methods 0.000 description 2
- 238000004886 process control Methods 0.000 description 2
- 238000005070 sampling Methods 0.000 description 2
- 230000009466 transformation Effects 0.000 description 2
- 241000195620 Euglena Species 0.000 description 1
- 229930012538 Paclitaxel Natural products 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 230000009172 bursting Effects 0.000 description 1
- 239000006285 cell suspension Substances 0.000 description 1
- 230000007423 decrease Effects 0.000 description 1
- 238000005243 fluidization Methods 0.000 description 1
- 238000009434 installation Methods 0.000 description 1
- 238000000034 method Methods 0.000 description 1
- 239000002101 nanobubble Substances 0.000 description 1
- 238000011022 operating instruction Methods 0.000 description 1
- 229960001592 paclitaxel Drugs 0.000 description 1
- 230000001737 promoting effect Effects 0.000 description 1
- 238000004062 sedimentation Methods 0.000 description 1
- 238000003756 stirring Methods 0.000 description 1
- RCINICONZNJXQF-MZXODVADSA-N taxol Chemical compound O([C@@H]1[C@@]2(C[C@@H](C(C)=C(C2(C)C)[C@H](C([C@]2(C)[C@@H](O)C[C@H]3OC[C@]3([C@H]21)OC(C)=O)=O)OC(=O)C)OC(=O)[C@H](O)[C@@H](NC(=O)C=1C=CC=CC=1)C=1C=CC=CC=1)O)C(=O)C1=CC=CC=C1 RCINICONZNJXQF-MZXODVADSA-N 0.000 description 1
- 210000003501 vero cell Anatomy 0.000 description 1
Images
Landscapes
- Apparatus Associated With Microorganisms And Enzymes (AREA)
- Micro-Organisms Or Cultivation Processes Thereof (AREA)
Abstract
本实用新型提供了一种低剪切力气升式发酵罐增氧与混合装置。该技术方案在气升式发酵罐中除配备进气空气分布器外,还加装多轮气石,可调整多轮气石与空气导流杯喷口方向调整气液流沿导流筒的循环方向。微气泡流喷射到发酵罐中后,形成的气液流在导流筒的引导下进行循环流动,实现发酵液与菌体的混匀。空气分布器安装于罐底放料口处,包括底部气石与金属盖片。气石喷出的纳米到微米级直径气泡高效增加发酵罐溶氧浓度,通过调节气石与空气分布器两者的进气量控制发酵液的溶氧水平与物料混匀。在保证发酵过程中溶氧水平的前提下,一方面大大降低能耗,另一方面降低了传统气升式发酵罐为提高溶氧剧烈通气对培养微生物或动植物细胞的剪切力损伤。
The utility model provides an oxygen-increasing and mixing device for a low-shear force air-lift fermenter. In this technical solution, in addition to the intake air distributor, the airlift fermentation tank is also equipped with multiple rounds of air stones, which can adjust the direction of the multi-round air stones and the spout of the air guide cup to adjust the circulation of the gas-liquid flow along the guide cylinder. direction. After the microbubble flow is sprayed into the fermentation tank, the formed gas-liquid flow circulates under the guidance of the guide tube to realize the mixing of the fermentation liquid and the bacteria. The air distributor is installed at the discharge port at the bottom of the tank, including the bottom air stone and metal cover. The nano-to-micron diameter bubbles ejected by the air stone can effectively increase the dissolved oxygen concentration of the fermentation tank, and the dissolved oxygen level of the fermentation liquid and the material mixing can be controlled by adjusting the air intake of the air stone and the air distributor. On the premise of ensuring the dissolved oxygen level in the fermentation process, on the one hand, the energy consumption is greatly reduced, and on the other hand, the shear force damage to the cultured microorganisms or animal and plant cells caused by the traditional airlift fermenter to increase the dissolved oxygen vigorous aeration is reduced.
Description
技术领域technical field
本实用新型属于一种生物工程领域,涉及气升式发酵罐发酵液增氧装置,尤其是对剪切力敏感的微藻细胞、动物细胞与植物细胞培养中增加氧气与促进物料混匀的装置。The utility model belongs to the field of biological engineering, and relates to an air-lift fermenter fermentation liquid oxygenation device, in particular to a device for increasing oxygen and promoting material mixing in the culture of shear-sensitive microalgae cells, animal cells and plant cells .
背景技术Background technique
气升式发酵罐具有结构简单,能耗低,供氧效率高,流化效率高等诸多优点。生物工业已经大量应用的气升式发酵罐有气升内环流发酵罐、气液双喷射气升环流发酵罐、设有多层分布板的塔式气升发酵罐。利用空气喷嘴喷出高速的空气,空气以气泡式分散于液体中,在通气的一侧,液体平均密度下降,在不通气的一侧,液体密度较大,因而产生与通气侧的液体产生密度差,从而形成发酵罐内液体的环流。但对于一些微藻细胞、动物细胞与植物原生质体等培养物,因细胞较大与没有细胞壁保护等原因,对剪切力比较敏感,传统气升式发酵罐为增加溶氧与物料混匀而加大的高速空气流对以上培养物会产生伤害,而限制了传统气升式发酵罐的在以上细胞培养中的适用性。The airlift fermentation tank has many advantages such as simple structure, low energy consumption, high oxygen supply efficiency and high fluidization efficiency. The air-lift fermenters that have been widely used in the biological industry include air-lift inner circulation fermenters, gas-liquid double jet air-lift circulation fermenters, and tower-type air-lift fermenters with multi-layer distribution plates. The high-speed air is sprayed from the air nozzle, and the air is dispersed in the liquid in the form of bubbles. On the ventilated side, the average density of the liquid decreases. On the non-ventilated side, the liquid density is higher, so the density of the liquid on the ventilated side is generated. difference, thereby forming a circulation of the liquid in the fermenter. However, for some cultures such as microalgae cells, animal cells and plant protoplasts, they are more sensitive to shear force due to the large cells and no cell wall protection. The increased high-speed air flow will cause damage to the above culture, which limits the applicability of the traditional airlift fermenter in the above cell culture.
经专利检索发现,气升式发酵罐改进集中于增加或改进搅拌装置与消泡等装置来提高溶氧效率与过程控制效率(如CN208151359U,CN208151345U,CN208151345U,CN209923330U, CN105219618B,CN112358952A,CN202576406U,CN211947007U,CN207646189U),或改进挡板或导流管结构增加环流与混合效率(如CN211522177U,CN210620795U, CN102796650A,CN111662803A,CN105039150B,CN209010511U,CN208667695U, CN210886007U),改进空气分布器结构(如CN204569910U,CN203754704U,CN102250752B, CN105602837A,CN210048760U,CN211847927U),增强发酵参数过程控制能力,如增加PLC 控制器或光、声、磁控系统(如CN108485951A,)或综合改造发酵罐结构增加混合效率 (CN209412225U)。以上气升式发酵罐为了增加溶氧与发酵液混合效率均导致了液体剪切力的增大,因此不适于对剪切力敏感的细胞发酵过程。Through patent search, it is found that the improvement of air-lift fermenters focuses on adding or improving stirring devices and defoaming devices to improve the efficiency of dissolved oxygen and process control (such as CN208151359U, CN208151345U, CN208151345U, CN209923330U, CN105219618B, CN112358952A, CN202576406U, CN211947U, CN207646189U),或改进挡板或导流管结构增加环流与混合效率(如CN211522177U,CN210620795U, CN102796650A,CN111662803A,CN105039150B,CN209010511U,CN208667695U, CN210886007U),改进空气分布器结构(如CN204569910U,CN203754704U,CN102250752B, CN105602837A , CN210048760U, CN211847927U), enhance the fermentation parameter process control ability, such as adding PLC controller or light, sound, magnetic control system (such as CN108485951A,) or comprehensively transform the structure of the fermentation tank to increase the mixing efficiency (CN209412225U). In order to increase the mixing efficiency of dissolved oxygen and fermentation broth, the above air-lift fermenters all lead to the increase of liquid shear force, so they are not suitable for the cell fermentation process that is sensitive to shear force.
本申请与上述专利相比,本申请采用可喷出纳米至微米级直径气泡的气石供气,在低强度通气的条件下,大大增加气液接触面,相比传统的气升式发酵罐,加装该实用新型后,在同等强度通气量的条件下,大大增加了气液接触面,显著提高溶氧效率,避免了通入高强度气流,从而避免了过高剪切力的发生;另一方面,通过引入底部气石,可大大增强发酵液的混合效率。气石的个数与固定气石的连接管轮数可根据发酵细胞的好氧程度进行调整,底部气体出口上方加一顶盖,引导气流方向,使沉降的细胞重新悬浮进入气液循环流。该气升式发酵罐增氧与混合装置可显著增加溶氧与混合效率,并大大降低空气压缩机能耗。Compared with the above-mentioned patents, the present application uses an air stone that can eject bubbles of nanometer to micrometer diameter for gas supply. Under the condition of low-intensity aeration, the gas-liquid contact surface is greatly increased. Compared with the traditional airlift fermentation tank , After the utility model is installed, under the condition of the same intensity of ventilation, the gas-liquid contact surface is greatly increased, the dissolved oxygen efficiency is significantly improved, and the introduction of high-intensity airflow is avoided, thereby avoiding the occurrence of excessive shear force; On the other hand, by introducing the bottom airstone, the mixing efficiency of the fermentation broth can be greatly enhanced. The number of air stones and the number of connecting tube rounds of the fixed air stones can be adjusted according to the aerobic degree of the fermenting cells. A top cover is added above the gas outlet at the bottom to guide the air flow direction, so that the settled cells can be resuspended into the gas-liquid circulation flow. The air-lift fermenter oxygenation and mixing device can significantly increase the dissolved oxygen and mixing efficiency, and greatly reduce the energy consumption of the air compressor.
实用新型内容Utility model content
本实用新型的目的是为传统气升式发酵罐提供一种高溶氧与混合效率,低剪切力、低改造成本、实用性强与低能耗、适用于微藻、动物与植物细胞发酵培养的装置。The purpose of the utility model is to provide a traditional air-lift fermenter with a high dissolved oxygen and mixing efficiency, low shear force, low transformation cost, strong practicability and low energy consumption, and is suitable for the fermentation culture of microalgae, animal and plant cells. installation.
本实用新型的解决技术问题的方案如下:The solution to the technical problem of the present invention is as follows:
一种低剪切力气升式发酵罐增氧与混合装置,其特征在于:包括环列气石(1)、连接管 (2)、气体导流杯(19)、单向气阀(10)、气体分布器(6)、底部气石(23)、螺纹(20)与耐热密封圈(21)。环列气石(1)与底部气石(23)为增氧气泡石或气盘石或鱼缸空气雾化器或增氧头或气泡盘或气盘或氧气泵沙头或纳米气盘石或纳米气泡石或高溶氧气饼或氧气石或其他由烧结形成的多孔石。环列气石(1)通过螺纹(20)垂直连接于连接管(2)上,气石头朝向可向上或向下或与罐底(3)平行或垂直。底部气石(23)通过螺纹(20)连接于连接管(2)出气端,气石头朝向金属盖片(24),连接管上设有单向气阀(6)。固定连接环列气石(1)或底部气石(23)与连接管(2)的螺纹(20)内有耐热密封圈(21)。环列气石(1) 与连接管之间有金属气体导流杯(19),根据所需气液混合液沿导流筒的循环流动方向,通过调整焊接在连接管上的螺纹的位置,调整气石头朝向与气体导流杯开口方向。气体导流杯(19) 底部中心有圆孔,套接固定在螺纹上。A low-shear force air-lift type fermenter oxygenation and mixing device, characterized in that it comprises a ring-shaped air stone (1), a connecting pipe (2), a gas guide cup (19), and a one-way air valve (10) , a gas distributor (6), a bottom air stone (23), a thread (20) and a heat-resistant sealing ring (21). The ring-column air stone (1) and the bottom air stone (23) are oxygen-enhancing air stones or air-pan stones or fish tank air atomizers or oxygen-increasing heads or bubble discs or air discs or oxygen pump sand heads or nano-aero-pan stones or nano-bubbles Stone or high dissolved oxygen cake or oxygen stone or other porous stone formed by sintering. The ring-column air stone (1) is vertically connected to the connecting pipe (2) through the thread (20), and the air stone can be oriented upward or downward or parallel or perpendicular to the tank bottom (3). The bottom air stone (23) is connected to the air outlet end of the connecting pipe (2) through threads (20), the air stone faces the metal cover sheet (24), and the connecting pipe is provided with a one-way air valve (6). A heat-resistant sealing ring (21) is arranged in the thread (20) for fixedly connecting the ring-column air stone (1) or the bottom air stone (23) and the connecting pipe (2). There is a metal gas guide cup (19) between the ring-shaped air stone (1) and the connecting pipe. According to the circulating flow direction of the required gas-liquid mixture along the guide cylinder, by adjusting the position of the thread welded on the connecting pipe, Adjust the direction of the gas stone and the opening of the gas guide cup. There is a round hole in the center of the bottom of the gas guide cup (19), which is sleeved and fixed on the thread.
优选的,固定环列气石(1)的连接管为两组。Preferably, there are two groups of connecting pipes for fixing the ring-column airstone (1).
优选的,每组连接管连接的环列气石(1)为8个。Preferably, there are 8 airstones (1) connected to each group of connecting pipes.
连接管上设有单向气阀。气体分布器(6)包括底部气石(23)、连接管(2)、螺纹(20)、耐热密封圈(21)、金属盖片(24)、单向气阀(10)与金属杆(22)。There is a one-way air valve on the connecting pipe. The gas distributor (6) comprises a bottom gas stone (23), a connecting pipe (2), a thread (20), a heat-resistant sealing ring (21), a metal cover sheet (24), a one-way gas valve (10) and a metal rod (twenty two).
优选的,罐底部的空气出口上方0.5cm固定一大于出气口直径的圆形金属盖片(24),圆形金属盖片(24)由三根金属杆(22)焊接固定于管底或空气出口上。起到导流空气的作用。Preferably, a circular metal cover sheet (24) larger than the diameter of the air outlet is fixed 0.5 cm above the air outlet at the bottom of the tank, and the circular metal cover sheet (24) is welded and fixed to the bottom of the pipe or the air outlet by three metal rods (22). superior. Play the role of guiding air.
本实用新型的有益效果如下:The beneficial effects of the present utility model are as follows:
1.本装置可装配于传统发酵罐上,改造成本低,实用性强,只需在现有供气系统上加装连接管、螺纹、气石、气垫、导流片、以及在底部空气分布器器上方焊接金属片即可。1. The device can be assembled on traditional fermentation tanks, with low cost of transformation and strong practicability. It only needs to add connecting pipes, threads, air stones, air cushions, guide plates, and air distribution at the bottom to the existing air supply system. Weld the metal sheet on the top of the device.
2.本装置喷出的气泡为纳米到微米级气泡,气液接触面积大大增加,在较低空气压力下即可有效提高发酵液溶氧,从而大大降低空压机能耗。因小气泡爆裂剪切力弱,因此大大降低对微藻细胞、动物细胞、植物细胞等对剪切力敏感培养物的损伤。2. The bubbles ejected by this device are nano- to micron-sized bubbles, and the gas-liquid contact area is greatly increased, and the dissolved oxygen of the fermentation liquid can be effectively increased under lower air pressure, thereby greatly reducing the energy consumption of the air compressor. Due to the weak shear force of small bubble bursting, the damage to shear stress-sensitive cultures such as microalgae cells, animal cells, and plant cells is greatly reduced.
3.本装置改造了传统气升式发酵罐底部的空气分布器,避免了较低空气压力下,气体混合作用变弱,细胞沉降的问题,达到既提高溶氧又保证物料混合的目的。3. The device modifies the air distributor at the bottom of the traditional air-lift fermenter, which avoids the problem of weak gas mixing and cell sedimentation under lower air pressure, and achieves the purpose of improving dissolved oxygen and ensuring material mixing.
附图说明Description of drawings
图1为安装于气升式发酵罐上的本实用新型结构示意图正视图;1 is a schematic front view of the structure of the present utility model installed on an air-lift fermenter;
图2为本实用新型中环列气石的结构示意图;Fig. 2 is the structural representation of the ring column air stone in the utility model;
图3为本实用新型中螺纹与耐热密封圈的结构示意图;Fig. 3 is the structural representation of thread and heat-resistant sealing ring in the utility model;
图4为本实用新型中气体分布器结构示意图;4 is a schematic structural diagram of a gas distributor in the utility model;
图5为安装于气升式发酵罐上的本实用新型结构示意图侧视图;5 is a side view of a schematic structural diagram of the present utility model installed on an airlift fermenter;
图6为安装于气升式发酵罐端盖结构示意图;;Fig. 6 is the structural representation of the end cover installed in the air-lift fermenter;
图中1.环列气石,2.连接管,3.罐底,4.导流筒,5.中部冷却夹套,6.气体分布器,7.出料口,8.出料口阀门,9.底部冷却夹套,10.单向气阀,11.补料口,12.接种口,13.温度计套管,14.传感器套管,15.传感器套管,16.视孔,17.取样管,18.法兰,19.气体导流杯,20.螺纹,21.耐热密封圈,22.金属杆,23.底部气石,24.金属盖片。In the figure, 1. Ring-column gas stone, 2. Connecting pipe, 3. Tank bottom, 4. Guide tube, 5. Middle cooling jacket, 6. Gas distributor, 7. Outlet, 8. Outlet valve , 9. Bottom cooling jacket, 10. One-way air valve, 11. Feeding port, 12. Inoculation port, 13. Thermometer sleeve, 14. Sensor sleeve, 15. Sensor sleeve, 16. Sight hole, 17 .Sampling tube, 18. Flange, 19. Gas guide cup, 20. Thread, 21. Heat-resistant sealing ring, 22. Metal rod, 23. Bottom air stone, 24. Metal cover.
具体实施方式Detailed ways
下面结合实施例对实用新型作进一步的说明,但本实用新型要求保护的范围并不限于实施例表达的范围。任何熟悉相关技艺者,在不脱离本实用新型的精神和范围内,当可略加改动与润饰。因此,本实用新型的专利保护范围视本说明书所附的申请专利范围所界定的为准。The utility model will be further described below in conjunction with the embodiments, but the scope of protection of the utility model is not limited to the scope expressed by the embodiments. Anyone who is familiar with the related art can make slight changes and modifications without departing from the spirit and scope of the present invention. Therefore, the scope of the patent protection of the present invention is determined by the scope of the patent application attached to this specification.
本实用新型所给出的低剪切力气升式发酵罐增氧与混合装置,是低剪切力细胞培养时用以提高气升式发酵罐溶氧与混合效率的装置。The low-shear-force air-lift fermentor oxygenation and mixing device provided by the utility model is a device used to improve the oxygen-dissolving and mixing efficiency of the air-lift fermenter during low-shear cell culture.
如图1-6,所述低剪切力气升式发酵罐增氧与混合装置安装于气升式发酵罐上,包括环列气石(1)、连接管(2)、气体导流杯(19)、单向气阀(10)、气体分布器(6)、底部气石(23)、螺纹(20)与耐热密封圈(21)。环列气石(1)与底部气石(23)为增氧气泡石。环列气石(1)通过螺纹(20)垂直连接于连接管(2)上,气石头朝下与罐底垂直。底部气石(23) 通过螺纹(20)连接于连接管(2)出气端,气石头朝向金属盖片(24),连接管上设有单向气阀(6)。固定连接环列气石(1)与底部气石(23)和连接管(2)的螺纹(20)内有耐热密封圈(21)。金属气体导流杯(19)底部有圆孔,套于连接环列气石(1)与连接管的螺纹上,环列气石与连接管连接紧密后,金属气体导流杯被夹紧固定。固定环列气石(1)的连接管为两组;每组连接管连接的环列气石(1)为8个。连接管上设有单向气阀。气体分布器(6) 包括底部气石(23)、连接管(2)、螺纹(20)、耐热密封圈(21)、金属盖片(24)、单向气阀(10)与金属杆(22)。罐底部的空气出口上方0.5cm处固定一大于出气口直径的圆形金属盖片(24),圆形金属盖片(24)由三根金属杆(22)焊接固定于管底或空气出口上。起到导流空气的作用。As shown in Figures 1-6, the low-shear air-lift fermenter oxygenation and mixing device is installed on the air-lift fermenter, and includes a ring-shaped air stone (1), a connecting pipe (2), a gas guide cup ( 19), one-way air valve (10), air distributor (6), bottom air stone (23), thread (20) and heat-resistant sealing ring (21). The ring column air stone (1) and the bottom air stone (23) are oxygen-enhancing air stones. The ring-column air stone (1) is vertically connected to the connecting pipe (2) through the thread (20), and the air stone faces downward and is perpendicular to the bottom of the tank. The bottom air stone (23) is connected to the air outlet end of the connecting pipe (2) through threads (20), the air stone faces the metal cover sheet (24), and the connecting pipe is provided with a one-way air valve (6). A heat-resistant sealing ring (21) is provided in the thread (20) for fixedly connecting the ring-column air stone (1) with the bottom air stone (23) and the connecting pipe (2). There is a round hole at the bottom of the metal gas guide cup (19), which is sleeved on the thread connecting the ring-shaped air stone (1) and the connecting pipe. After the ring-shaped air stone and the connecting pipe are tightly connected, the metal gas guide cup is clamped and fixed. . There are two groups of connecting pipes for fixing the ring-shaped air stones (1); and eight ring-shaped air stones (1) are connected to each group of connecting pipes. There is a one-way air valve on the connecting pipe. The gas distributor (6) includes a bottom gas stone (23), a connecting pipe (2), a thread (20), a heat-resistant sealing ring (21), a metal cover sheet (24), a one-way gas valve (10) and a metal rod (twenty two). A circular metal cover sheet (24) larger than the diameter of the air outlet is fixed at 0.5cm above the air outlet at the bottom of the tank, and the circular metal cover sheet (24) is welded and fixed on the bottom of the tube or the air outlet by three metal rods (22). Play the role of guiding air.
上述气升式发酵罐,除所述低剪切力气升式发酵罐增氧与混合装置外,还包括罐体,导流筒(4),中部冷却夹套(5),出料口(7),出料口阀门(8),底部冷却夹套(9),补料口(11),接种口(12),温度计套管(13),pH传感器套管(14),溶氧传感器套管(15),视孔(16),取样管(17),法兰(18)。The above-mentioned air-lift fermenter, in addition to the low-shear force air-lift fermenter oxygenation and mixing device, also comprises a tank body, a guide tube (4), a middle cooling jacket (5), a discharge port (7 ), outlet valve (8), bottom cooling jacket (9), feeding port (11), inoculation port (12), thermometer sleeve (13), pH sensor sleeve (14), dissolved oxygen sensor sleeve Tube (15), sight hole (16), sampling tube (17), flange (18).
本装置适于发酵工业中无细胞壁的微藻、动物细胞,如与植物原生质体等对剪切力敏感的培养物,如纤细裸藻、Vero细胞、紫杉醇原生质体等。The device is suitable for microalgae and animal cells without cell walls in the fermentation industry, such as shear-sensitive cultures such as plant protoplasts, such as Euglena slenderum, Vero cells, and paclitaxel protoplasts.
本装置运行说明如下:The operating instructions of this device are as follows:
如图1、2、4,无菌压缩空气由连接管通入发酵罐内,经环列气石与底部气石扩散,形成的微小气泡与发酵液混合后形成低密度气液混合体;环列气石喷出气泡喷到罐底后,反流后进入导流筒与罐壁之间的通道内向上运动,导流筒中心的发酵液下沉,形成环流,实现发酵液的混合;底部气石喷出的微小气泡与发酵液混合后向上运动,被金属盖片导流后沿罐底方向运动,与环列气石形成的气液流混合,将沉降于罐底与出料口中的细胞重新悬浮混合。As shown in Figures 1, 2, and 4, sterile compressed air is introduced into the fermentation tank through the connecting pipe, diffused by the ring-shaped air stone and the bottom air stone, and the formed tiny air bubbles are mixed with the fermentation liquid to form a low-density gas-liquid mixture; After the air bubbles are sprayed to the bottom of the tank, the gas flows back into the channel between the diversion cylinder and the tank wall and moves upward, and the fermentation liquid in the center of the diversion cylinder sinks to form a circulation to realize the mixing of the fermentation liquid; The tiny bubbles ejected from the air stone mix with the fermentation liquid and then move upward, and then move along the direction of the bottom of the tank after being diverted by the metal cover sheet. Cells are resuspended and mixed.
根据溶氧传感器(15)的读数,在固定底部气石(23)的连接管(2)通气量的情况下,调节环列气石(1)连接管(2)通气的组数与每组连接管的通气量大小来控制发酵液溶氧水平。在需要低溶氧情况下,停止环列气石(1)连接管(2)供气,调节底部气石(23)连接管(2)的通气量来控制溶氧水平与物料混合以及细胞悬浮。According to the reading of the dissolved oxygen sensor (15), under the condition that the ventilation volume of the connecting pipe (2) of the bottom air stone (23) is fixed, adjust the number of ventilation groups of the connecting pipe (2) of the annular air stone (1) and the ventilation rate of each group. The ventilation volume of the connecting pipe is used to control the dissolved oxygen level of the fermentation broth. When low dissolved oxygen is required, stop the air supply to the connecting pipe (2) of the ring-column air stone (1), and adjust the ventilation rate of the connecting pipe (2) of the bottom air stone (23) to control the level of dissolved oxygen and the material mixing and cell suspension. .
以上所述仅是本实用新型的优选实施方式,应当指出,对于本技术领域的普通技术人员来说,在不脱离本实用新型原理的前提下,还可以做出若干改进和润饰,这些改进和润饰也应视为本实用新型的保护范围。The above is only the preferred embodiment of the present invention. It should be pointed out that for those skilled in the art, without departing from the principle of the present invention, several improvements and modifications can be made. These improvements and Retouching should also be regarded as the protection scope of the present invention.
Claims (11)
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN202120554944.9U CN216274173U (en) | 2021-03-18 | 2021-03-18 | A low-shear air-lift fermenter oxygenation and mixing device |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN202120554944.9U CN216274173U (en) | 2021-03-18 | 2021-03-18 | A low-shear air-lift fermenter oxygenation and mixing device |
Publications (1)
Publication Number | Publication Date |
---|---|
CN216274173U true CN216274173U (en) | 2022-04-12 |
Family
ID=81001684
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN202120554944.9U Active CN216274173U (en) | 2021-03-18 | 2021-03-18 | A low-shear air-lift fermenter oxygenation and mixing device |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN216274173U (en) |
-
2021
- 2021-03-18 CN CN202120554944.9U patent/CN216274173U/en active Active
Similar Documents
Publication | Publication Date | Title |
---|---|---|
WO2018076414A1 (en) | Airlift reactor with helical porous sieve plate | |
US9499290B2 (en) | Stationary bubble reactors | |
CN101985595A (en) | Membrane type photobioreactor for enhancing microalgae culturing | |
CN105505749A (en) | Air-liquid dual injection type airlift loop reactor | |
CN112939212A (en) | Device and method for enhancing aeration by utilizing micro-bubbles generated by hydraulic shearing | |
CN112939211B (en) | Device and method for enhancing aeration by utilizing hydraulic shearing and gas buoyancy | |
WO2019162971A1 (en) | An improved aeration system for bioreactor, fermenter and process vessel | |
CN107904144B (en) | Aeration flow disturbing device of microalgae column type reactor | |
CN203728638U (en) | MBBR (moving bed biofilm reactor) integrated autotrophic nitrogen removal device | |
CN216274173U (en) | A low-shear air-lift fermenter oxygenation and mixing device | |
CN114563543B (en) | An intelligent experimental device for dissolved oxygen | |
CN102603063A (en) | Jet aerator for oxygenating in water | |
CN101306879A (en) | Three-phase fluidized algae photobioreactor system for treating high-concentration organic wastewater | |
CN212375263U (en) | Photobioreactor for Microalgae Cultivation | |
CN205528736U (en) | Two formula gas lift formula circulation flow reactor that spout of gas -liquid | |
CN205635573U (en) | Horizontal inside and outside dual cycle airlift bioreactor | |
CN105481054B (en) | A kind of injection circulation reactor with guide way component | |
WO2012053912A1 (en) | Method of provision of silicate to culture media | |
CN207581784U (en) | A kind of new and effective bioreactor | |
CN216336880U (en) | Liftable alternative stirring, oxygenating and aerating system | |
CN108251286B (en) | Gas-liquid atomization efficient bioreactor | |
CN105293678A (en) | Blocking-proof micro-bubble aeration device for sewage treatment | |
CN201722206U (en) | Novel deep-level split-type external circulating biological film reactor | |
CN115820405A (en) | A bubble jet coupled impinging flow enhanced aerobic fermentation process device | |
CN222923137U (en) | A special air distributor for xanthan gum fermentation tank |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
GR01 | Patent grant | ||
GR01 | Patent grant | ||
TR01 | Transfer of patent right | ||
TR01 | Transfer of patent right |
Effective date of registration: 20240708 Address after: 1st Floor, Electronic Packaging Workshop, Baoshida Group Industrial Park, No. 8 Kaiyuan Road, East Section of Gongye North Road, Licheng District, Jinan City, Shandong Province, 250001 Patentee after: Shandong nameida Biotechnology Co.,Ltd. Country or region after: China Address before: 300457 Tianjin Binhai New Area Economic and Technological Development Zone thirteenth Avenue 29 Patentee before: TIANJIN University OF SCIENCE AND TECHNOLOGY Country or region before: China |