Cryogenic Liquid Buffering for Stable Argon Distillation Feed

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Solution Overview

Problem

Air separation units with argon production experience significant flow disturbances due to the need for additional pressurization of bottles, which cannot be compensated without specifying additional flow on the main air compressor, leading to instability and increased costs.

Innovation Solution

A cryogenic distillation device with a cryogenic liquid tank and reboiler system that compensates for the lack of flow by sending cryogenic liquid and vaporized liquid to columns during pressurization phases, allowing for flexible energy optimization and reduced compressor sizing.

Engineering Contradictions & Design Principles

VSEngineering Contradiction Analysis

1Quantity of substance

If the main air compressor is sized to provide additional flow for bottle pressurization, then the pressurization flow requirement is met, but the compressor cost and energy consumption increase

Engineering Contradiction:
Improvecompressor flow capacityVSAvoidcompressor energy consumption
Core Design Contradiction:
Quantity of substanceVSUse of energy by stationary object

Solution Approach 1:

The purification bottles operate in cyclic alternating phases: one bottle performs adsorption while the other undergoes pressurization and regeneration. This periodic operation allows the compressor to supply feed flow to columns during adsorption phases and pressurization flow during regeneration phases, rather than requiring continuous additional flow capacity

Inventive Principle:
Principle #19Periodic action

Solution Approach 2:

The cryogenic liquid tank continuously supplies liquid to the columns during pressurization phases, ensuring uninterrupted feed to the distillation columns. This continuous useful action compensates for the temporary reduction in compressor feed flow, maintaining column operation stability without requiring oversized compressor capacity

Inventive Principle:
Principle #20Continuity of useful action

2Ease of manufacture

If the main air compressor is sized for nominal flow without additional pressurization capacity, then compressor cost is reduced, but flow stability to columns deteriorates during pressurization phases

Engineering Contradiction:
Improvecompressor sizing costVSAvoidcolumn feed flow stability
Core Design Contradiction:
Ease of manufactureVSStability of the object's composition

Solution Approach 1:

The cryogenic liquid tank acts as an intermediary storage device between the compressor and the distillation columns. During pressurization phases when compressor feed flow to columns is reduced, the tank releases stored liquid to maintain stable column feed rates. This intermediary buffer decouples the compressor operation from column feed requirements

Inventive Principle:
Principle #24Intermediary (Mediator)

Solution Approach 2:

The system changes the physical state and timing of liquid supply by storing cryogenic liquid during non-pressurization phases and releasing it during pressurization phases. This parameter change in supply timing compensates for flow disturbances without requiring compressor modification

Inventive Principle:
Principle #35Parameter changes

3Stability of the object's composition

If a tank sends liquid to columns during pressurization phases, then column feed stability is maintained, but the device complexity increases

Engineering Contradiction:
Improvecolumn feed flow stabilityVSAvoidsystem structure complexity
Core Design Contradiction:
Stability of the object's compositionVSDevice complexity

Solution Approach 1:

The cryogenic liquid tank serves multiple functions: it stores cryogenic liquid, acts as a buffer to stabilize column feed during pressurization phases, and can be integrated with the existing cold box structure. This multi-functionality justifies the added complexity by providing several benefits from a single component

Inventive Principle:
Principle #6Universality (Multi-functionality)

Solution Approach 2:

The tank system is integrated with the existing purification and distillation equipment, merging the storage function with the feed supply system. The reboiler and tank are thermally coupled, and the liquid supply system is combined with the existing column feed infrastructure, reducing overall system complexity

Inventive Principle:
Principle #5Merging (Combining)

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 reduces the cost and energy consumption of air separation units by maintaining system stability and flexibility, especially in argon production scenarios, without requiring additional compressor flow.

Implementation Method 1

a reboiler in the tank to vaporize the liquid contained therein

Methodology Applied
Scientific EffectVaporization: Evaporation

Implementation Method 2

means for sending a warming gas to the reboiler

Methodology Applied
Scientific EffectHeating: Heating

Implementation Method 3

A cryogenic liquid is a liquid at a temperature below 200 K

Methodology Applied
Scientific EffectCryogenic cooling: Cryogenics

Implementation Method 4

a purification unit for purifying the gas mixture in a system based on several bottles of adsorbent, operating according to a cycle comprising a pressurization phase

Methodology Applied
Scientific EffectAdsorption: Adsorption

Data Source

PatentUS8713964B2Method and device for separating a gas mixture by cryogenic distillation
Publication Date: 2014.05.06 LAIR LIQUIDE SA POUR LETUDE & LEXPLOITATION DES PROCEDES GEORGES CLAUDE
  • US8713964B2 patent drawing
  • US8713964B2 patent drawing

AI summary

The invention relates to a cryogenic distillation apparatus for a gas mixture, including a purification apparatus for purifying a gas mixture in a system with a plurality of adsorbant bottles, a column system, a capacity, means for feeding a cryogenic liquid to the capacity, means for feeding a vaporized liquid from the capacity to a column of the system, a vaporizer in the capacity for vaporizing the contained liquid; means for feeding a calorigenic gas to the vaporizer, and means for drawing a liquid from the capacity.