VPSA Oxygen Production Cycle Segmentation

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Solution Overview

Problem

Current oxygen production from atmospheric air using VPSA units is energy-inefficient, with high energy consumption being a significant cost factor due to the need for numerous cycles and complex flow management, especially in systems with short cycle times or multiple adsorbers.

Innovation Solution

A VPSA process with a specific pressure cycle involving multiple adsorbers, where three successive oxygen-rich gas streams of decreasing purity are produced, and repressurization is achieved using streams of increasing oxygen content, optimizing energy use by simplifying the cycle and reducing the number of intermediate steps.

Engineering Contradictions & Design Principles

VSEngineering Contradiction Analysis

1Loss of energy

If numerous cycles and complex flow management are used in VPSA units, then oxygen purity levels are maintained, but energy consumption increases significantly

Engineering Contradiction:
Improveenergy consumptionVSAvoidoxygen production efficiency
Core Design Contradiction:
Loss of energyVSProductivity

Solution Approach 1:

The patent segments the oxygen production process into three distinct streams of decreasing purity, each serving specific purposes in the cycle. This segmentation allows optimized use of each stream - the highest purity stream for product output, the second stream for repressurization, and the third stream for elution - thereby reducing overall energy consumption while maintaining productivity

Inventive Principle:
Principle #1Segmentation

Solution Approach 2:

The patent applies multi-functionality by using the oxygen-rich gas streams for multiple purposes within the same system. The streams serve both as product output and as repressurization/gas source for subsequent cycles, eliminating the need for separate compression steps and reducing energy requirements while maintaining continuous production

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

2Productivity

If the number of adsorbers is increased to improve oxygen production capacity, then productivity increases, but device complexity and energy consumption increase

Engineering Contradiction:
Improveoxygen production capacityVSAvoidsystem complexity
Core Design Contradiction:
ProductivityVSDevice complexity

Solution Approach 1:

The patent merges multiple functions into a simplified adsorber configuration. By using just one or two adsorbers that perform both separation and provide multiple gas streams through controlled depressurization, the system achieves high productivity without the complexity of coordinating numerous adsorbers in traditional multi-bed configurations

Inventive Principle:
Principle #5Merging (Combining)

3Productivity

If short cycle times are used to increase production rate, then productivity improves, but energy consumption and flow management complexity increase

Engineering Contradiction:
Improveproduction rateVSAvoidenergy consumption per unit time
Core Design Contradiction:
ProductivityVSLoss of energy

Solution Approach 1:

The patent ensures continuity of useful action by maintaining constant pressure during the oxygen production phase and using controlled depressurization to generate useful gas streams. This continuous operation at optimized pressure points maintains high production rates while minimizing energy consumption associated with frequent pressure cycling

Inventive Principle:
Principle #20Continuity of useful action

4Manufacturing precision

If traditional VPSA cycles with multiple intermediate steps are used, then oxygen purity is maintained, but energy consumption and cycle time increase

Engineering Contradiction:
Improveoxygen purityVSAvoidenergy consumption
Core Design Contradiction:
Manufacturing precisionVSLoss of energy

Solution Approach 1:

The patent applies preliminary action by pre-establishing the three oxygen-rich streams during the adsorption and depressurization phases before product extraction begins. This allows the system to maintain high oxygen purity through controlled stream selection while reducing the number of intermediate purification steps required, thereby lowering energy consumption

Inventive Principle:
Principle #10Preliminary action

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 process reduces energy consumption by streamlining the oxygen production cycle, allowing for more efficient use of adsorbers and energy resources, thereby lowering production costs while maintaining desired oxygen purity levels.

Implementation Method 1

a production step a) of a first oxygen-rich gas stream (T1) while loading upstream the adsorber with the atmospheric air stream

Methodology Applied
Scientific EffectAdsorption: Adsorption

Implementation Method 2

a production step b) of a second oxygen-rich gas stream (T2) by depressurization of the adsorber bed

Methodology Applied
Scientific EffectDesorption: Desorption

Data Source

PatentEP3274073B1Method for producing oxygen by vpsa
Publication Date: 2020.10.14 LAIR LIQUIDE SA POUR LETUDE & LEXPLOITATION DES PROCEDES GEORGES CLAUDE
  • EP3274073B1 patent drawing
  • EP3274073B1 patent drawing
  • EP3274073B1 patent drawing

AI summary

The invention relates to a method for producing oxygen by adsorbing a stream of atmospheric air, using a VPSA unit comprising at least one adsorber, each adsorber undergoing a single pressure cycle comprising the following steps: a) producing a first stream of gas having an oxygen content T1 while loading the adsorber of the stream of atmospheric air upstream; b) producing a second stream of gas comprising an oxygen content T2 < T1; c) producing a third stream of gas comprising an oxygen content T3 < T2 < T1 while simultaneously extracting a nitrogen-enriched residual stream; d) eluting the adsorber, from which the three streams of gas produced in steps a), b) and c) are taken, exclusively via the second stream of gas produced in step b); e) repressuring the adsorber that underwent the elution of step d) consecutively with at least two streams, first and second repressuring streams, with increasing oxygen content, the first repressuring stream being the third stream of gas produced in step c) and the second repressuring stream being the second stream of gas produced in step b).