A high-efficiency dissolved oxygen stirrer for a fermentation tank and a fermentation tank
A fermenter and agitator technology, applied in the field of fermenters, can solve the problems of low specific gravity of gas, destruction of bacteria in fermenters, low efficiency of dissolved oxygen, etc., and achieve the effect of reducing shear damage.
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Embodiment 1
[0033] see figure 2 As shown, it is a fermentor high-efficiency dissolved oxygen stirrer 10 according to a preferred embodiment of the present invention, which is installed in the fermenter 20 and includes a stirring shaft 11, and the stirring shaft 11 is installed at an inclination angle α relative to the central axis L of the fermenter In the fermentation tank 20, the inclination angle α is 1-2° or 2-4° or 4-5°, such as figure 2 2° shown.
[0034] combine figure 1 , Figure 4 , Figure 5 As shown, the agitator 10 also includes a multi-layer blade 12, which is a multi-layer propeller blade. The multi-layer propeller blade 12 is that the blades 121 of each layer are arranged in one layer along the helical line, but each layer is separated (such as Figure 4 ); or each blade 121 is arranged in a form that is connected end-to-end from top to bottom (such as Figure 5 ), the paddle 12 can be provided with 1-10 layers, preferably 2-5 layers. Preferably, each layer of blad...
Embodiment 2
[0038] see image 3As shown, it is a fermentor high-efficiency dissolved oxygen stirrer 10 according to a preferred embodiment of the present invention, which is installed in the fermenter 20 and includes a stirring shaft 11, and the stirring shaft 11 is relatively offset from the central axis L of the fermenter and is installed in the fermenter. In 40, the deviation D is about 2% to 3% or 3 to 4% of the diameter of the fermenter, more preferably 1 / 40.
[0039] combine figure 1 , Figure 4 , Figure 5 As shown, the agitator 10 of this embodiment includes a multi-layer blade 12, and the blade 12 is a multi-layer propeller blade. The multi-layer propeller blade 12 is that the blades 121 of each layer are arranged in one layer along the helical line, but each layer is separated (such as Figure 4 ); or each blade 121 is arranged in a form that is connected end-to-end from top to bottom (such as Figure 5 ), the paddle 12 can be provided with 1-10 layers, preferably 2-5 layer...
Embodiment 3
[0044] Regarding the structural design, size, rotational speed, etc. of the paddle 12 and the blade 121 in this embodiment, reference may be made to Embodiment 1-2. In this embodiment, on the basis of the above-mentioned embodiment, the stirring shaft 11 is deviated from the central axis L of the fermenter by a certain distance and is installed at an inclination angle α relative to the central axis L, and the inclination angle is 1-2° or 2-4° Or 4 to 5°, and the deviation distance D is about 2% to 3% or 3 to 4% of the diameter of the fermenter.
[0045] Since these two technical features can be combined without contradicting, contradicting or canceling each other, the technical effects and working principles of this embodiment can be superimposed with the relevant descriptions of Embodiments 1-2, which are not included here. Repeat.
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