Cryogenic Distillation Column Reflux for Peak Nitrogen Demand
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Solution Overview
Problem
Conventional air separation processes using cryogenic distillation face high costs due to prohibitive investment and labor costs for autonomous production units, and inefficient energy use in vaporizing liquid nitrogen for peak demand, leading to significant refrigeration energy loss.
Innovation Solution
Recover refrigeration power by redirecting vaporized liquid nitrogen to the distillation column during peak consumption, increasing reflux and allowing for additional nitrogen production, which is then stored to reduce or eliminate the need for conventional liquid nitrogen injection, thereby reducing operating costs.
Engineering Contradictions & Design Principles
Engineering Contradiction Analysis
1Quantity of substance
If liquid nitrogen is vaporized in an atmospheric heater to top up nitrogen molecules during peak consumption, then nitrogen demand is met, but refrigeration energy is lost
Solution Approach 1:
The invention converts the harmful energy loss from vaporizing liquid nitrogen in an atmospheric heater into a beneficial process by redirecting the liquid nitrogen through the distillation column where it is efficiently vaporized, transforming the waste refrigeration energy loss into useful cooling effect that maintains column temperature and produces additional nitrogen.
2Temperature
If liquid nitrogen is continuously injected to keep the apparatus cold, then refrigeration is maintained, but operating costs increase
Solution Approach 1:
The distillation column serves itself by using the incoming liquid nitrogen feed as both a cooling agent and a production feedstock. The liquid nitrogen vaporizes within the column, providing the necessary refrigeration to maintain low temperatures while simultaneously contributing to nitrogen production, eliminating the need for separate liquid nitrogen injection for cooling purposes.
3Stability of the object's composition
If the distillation column operates at nominal extraction level, then steady production is maintained, but additional nitrogen cannot be produced during peak demand
Solution Approach 1:
The invention introduces dynamic operation to the distillation column by allowing the liquid nitrogen feed rate to vary according to demand. During peak consumption, the liquid nitrogen feed is increased and redirected through the column, enabling the system to dynamically adjust production capacity while maintaining stable operation through controlled reflux adjustments.
4Quantity of substance
If an evaporator with large capacity is used to meet nitrogen demand, then nitrogen availability is improved, but investment cost and energy efficiency worsen
Solution Approach 1:
The distillation column is made multi-functional by serving both as the primary nitrogen production unit and as an emergency vaporizer for liquid nitrogen. This eliminates the need for a separate large-capacity evaporator, as the column can handle both steady-state production and peak-demand vaporization functions, reducing overall system complexity and investment cost.
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 approach significantly reduces operating costs by minimizing liquid nitrogen consumption and maintaining apparatus refrigeration using stored rich liquid, allowing for flexible production to meet variable demands without continuous liquid injection.
Implementation Method 1
In the distillation column, this inflow of liquid increases the level of reflux into the column... The column therefore acts as a 'vaporizer' for liquid coming from the storage tank.
Implementation Method 2
The present invention relates to an air separation process and apparatus using cryogenic distillation.
Data Source
AI summary
An air distillation unit comprises an air distillation column (10) suitable for producing a nominal flow of gaseous nitrogen, the top of said column being connected to a liquid nitrogen source (8), and operates by carrying out the following steps: a flow of compressed, cooled and purified air is sent to an exchanger (11) and then to the column, a flow of gaseous nitrogen is withdrawn from the column, the level of liquid at the bottom of the column is controlled; and injection liquid (20), sent from the source to the column, is no longer sent if the required production reduces to at most the nominal production. Application to the separation of air by cryogenic distillation.


