Fermentation Vessel Hydrodynamic Seal for Oxygen Transfer
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Solution Overview
Problem
Conventional fermentation apparatuses face challenges in maintaining efficient oxygen transfer during submerged fermentation due to bubble coagulation, which can be mitigated by anticoagulation chemicals or high-speed stirring, but these solutions either affect product quality or incur high energy costs.
Innovation Solution
A low-speed stirrer system with a hydrodynamic seal assembly that introduces processing gas through a shaft with rotating sealing rings, creating small bubbles and enhancing gas/liquid interface at low speeds, suitable for small-scale fermentation vessels.
Engineering Contradictions & Design Principles
Engineering Contradiction Analysis
1Productivity
If high-speed stirring is used to break up coagulated bubbles, then oxygen transfer efficiency is improved, but energy consumption increases and cell cultures may be damaged
Solution Approach 1:
The aeration system is segmented into multiple levels with separate aeration rings at different heights in the vessel. Each ring creates bubbles at a specific location, distributing the aeration function across multiple segments rather than relying on a single high-speed stirrer. This segmentation allows effective oxygen transfer without the need for high-speed mixing throughout the entire vessel.
Solution Approach 2:
A stationary screen or mesh structure is introduced as an intermediary element between the gas source and the liquid medium. This screen breaks up large bubbles into smaller bubbles passively as gas passes through it, eliminating the need for mechanical high-speed stirring. The screen acts as a mediator that achieves bubble breakup without direct mechanical intervention.
2Productivity
If high-speed stirring is used to break up coagulated bubbles, then oxygen transfer efficiency is improved, but cell culture integrity deteriorates
Solution Approach 1:
The aeration system is segmented into multiple levels with separate aeration rings at different heights in the vessel. Each ring creates bubbles at a specific location, distributing the aeration function across multiple segments rather than relying on a single high-speed stirrer. This segmentation allows effective oxygen transfer without the need for high-speed mixing throughout the entire vessel.
Solution Approach 2:
A stationary screen or mesh structure is introduced as an intermediary element between the gas source and the liquid medium. This screen breaks up large bubbles into smaller bubbles passively as gas passes through it, eliminating the need for mechanical high-speed stirring. The screen acts as a mediator that achieves bubble breakup without direct mechanical intervention.
3Productivity
If anticoagulation chemicals are used to prevent bubble coagulation, then oxygen transfer efficiency is improved, but product quality deteriorates
Solution Approach 1:
A stationary screen or mesh structure is introduced as an intermediary element between the gas source and the liquid medium. This screen breaks up large bubbles into smaller bubbles passively as gas passes through it, eliminating the need for chemical anticoagulants. The screen acts as a physical mediator that achieves bubble breakup without introducing harmful chemicals into the fermentation process.
Solution Approach 2:
The patent replaces chemical methods (anticoagulation chemicals) with a physical method (stationary screen or mesh structure) to achieve the same effect of preventing bubble coagulation. This substitution eliminates chemical contamination risks while maintaining oxygen transfer efficiency.
4Productivity
If rapid stirring is used to prevent bubble coagulation, then oxygen transfer efficiency is improved, but cooling requirements increase
Solution Approach 1:
The aeration system is segmented into multiple levels with separate aeration rings at different heights in the vessel. Each ring creates bubbles at a specific location, distributing the aeration function across multiple segments rather than relying on a single high-speed stirrer. This segmentation allows effective oxygen transfer without the need for high-speed mixing throughout the entire vessel, thereby reducing heat generation.
Solution Approach 2:
A stationary screen or mesh structure is introduced as an intermediary element between the gas source and the liquid medium. This screen breaks up large bubbles into smaller bubbles passively as gas passes through it, eliminating the need for mechanical high-speed stirring. The screen acts as a mediator that achieves bubble breakup without direct mechanical intervention, avoiding the heat generation associated with rapid stirring.
Applied Scientific Principles
This section explains which scientific principles are used to turn an abstract innovation direction into a practical engineering solution.
Function Achieved in This Case
This solution increases oxygen transfer rates at low energy costs without contaminating the product, maintaining optimal operating temperatures and being cost-effective for small-scale operations.
Implementation Method 1
resiliently biased towards one another, so that a sealing face of the first sealing ring may be biased into engagement with a sealing face of the second sealing ring
Implementation Method 2
the grooves, which will provide hydrodynamic separation of the sealing faces upon rotation of the shaft, allowing processing gas in the chamber to flow inwardly across the sealing faces
Implementation Method 3
the dam formation on the one sealing face will sealingly engage the other sealing face
Data Source
Figure 1
Figure 2~4
AI summary
A fermentation apparatus (10) with a fermentation vessel (12) having a low speed stirrer, the stirrer comprising a shaft (14) entering the vessel through an aperture (16) in the bottom of the vessel, one or more stirring elements (18) being mounted on the shaft for rotation therewith within the vessel; a seal (20) being provided to seal the gap between the shaft and aperture, the seal being located in a cylindrical housing attached to the bottom of the vessel, the seal having first and second seal assemblies (30, 50) spaced axially of one another to define a chamber (64) therebetween, an inlet (66) opening into said chamber for connection of the chamber to a supply of processing gas, the first seal assembly (30) being located between the fermentation vessel and the chamber comprising a seat (32) mounted on the shaft for rotation therewith and a mating ring mounted (36) in fixed rotational relationship but moveably axially of the housing, a sealing face (44) of the mating ring being resiliently biased into engagement with a sealing face (42) of the seat, the sealing face of one of the mating ring or the seat having grooves (68) , which will provide hydrodynamic separation of the sealing faces upon rotation of the shaft .