VPSA Pressure Swing Adsorption Oxygen Generator

Yipu VPSA (Vacuum Pressure Swing Adsorption) Oxygen Generator has successfully addressed the economic challenges of medium-scale oxygen demand scenarios through innovations in vacuum adsorption technology. Its core value lies in: providing one of the optimal technical paths for oxygen demand of 50-6000 Nm³/h, reducing the comprehensive operating cost by 35-50% compared with traditional solutions, significantly…

Yipu VPSA (Vacuum Pressure Swing Adsorption) Oxygen Generator has successfully addressed the economic challenges of medium-scale oxygen demand scenarios through innovations in vacuum adsorption technology. Its core value lies in: providing one of the optimal technical paths for oxygen demand of 50-6000 Nm³/h, reducing the comprehensive operating cost by 35-50% compared with traditional solutions, significantly lowering labor costs through an intelligent operation and maintenance system, and perfectly matching various application scenarios with a modular design. This equipment is particularly suitable for metallurgical enterprises undergoing energy-saving transformation, new sewage treatment projects, and distributed energy stations, and is one of the core equipment for achieving low-carbon production.

I. Market Pain Point Analysis

High Cost of Traditional Oxygen Supply Modes

  • Transportation and storage costs of liquid oxygen storage tanks and bottled oxygen account for more than the value of oxygen itself.
  • Cryogenic air separation equipment requires high investment intensity (investment per cubic meter of oxygen exceeds 3,000 yuan), suitable for large-scale centralized oxygen supply.

Prominent Energy Efficiency Bottlenecks

  • The power consumption of traditional PSA oxygen generation is as high as 0.45-0.55 kWh/Nm³.
  • Cryogenic oxygen generation has a long startup time (8-12 hours) and cannot adapt to load fluctuations.

Difficulties in Matching Medium-Scale Demand

  • There is a supply gap for medium-scale demand of 5-6000 Nm³/h.
  • Existing equipment lacks economical solutions in the purity range of 70%-94%.

High Requirements for Operation and Maintenance Support

  • Traditional equipment has low automation and requires professional technical personnel on duty.
  • Molecular sieves have a short service life (usually 2-3 years) and high replacement costs.

II. System Process Flow

Core System Configuration

  • Power System: Roots blower + roots vacuum pump unit
  • Separation System: Dual-tower/multi-tower adsorber (filled with lithium-based molecular sieves)
  • Control System: PLC + pneumatic switching valve group
  • Gas Storage System: Oxygen balance tank + pressure buffer device

Five-Step Cycle Process

  1. Pressurized Adsorption Stage
    • Roots blower pressurizes filtered air to 25-35 kPa.
    • Air enters the adsorber, and molecular sieves preferentially adsorb nitrogen (kinetic diameter 3.64 Å).
    • The purity of the produced oxygen gradually increases to the set value.
  2. Pressure Equalization and Depressurization Stage
    • The oxygen-rich gas (0.2-0.3 MPa) in the adsorber is introduced into the regeneration tower.
    • Recovers more than 85% of pressure energy and reduces system energy consumption.
  3. Vacuum Desorption Stage
    • Roots vacuum pump evacuates the tower pressure to -65~-75 kPa.
    • The adsorbed nitrogen, CO₂, and water molecules are completely desorbed.
  4. Pressure Equalization and Pressurization Stage
    • Uses oxygen-rich gas from other towers for pre-pressurization to reduce blower energy consumption.
  5. Product Gas Pressurization Stage
    • Oxygen booster increases the product gas pressure to 0.4-0.8 MPa.
    • Enters the balance tank to stabilize pressure fluctuations.

III. In-Depth Analysis of Technical Principles

Molecular Sieve Adsorption Mechanism

  • Adopts LiX-type lithium-based molecular sieves with an N₂/O₂ separation coefficient of 4.5-5.2.
  • Based on the strong interaction between the nitrogen quadrupole moment effect (1.3×10⁻²⁶ esu·cm²) and molecular sieve cations.
  • Oxygen molecules (without dipole moment) are basically not adsorbed, achieving efficient separation.

Vacuum-Enhanced Regeneration

  • The relationship between vacuum degree and nitrogen desorption capacity is exponential (desorption rate reaches 92% at -65 kPa).
  • Saves 25-35% more energy than traditional PSA and improves molecular sieve utilization by 40%.

IV. Core Competitive Advantages

Industry-Leading Energy Consumption Indicators

  • Unit power consumption: 0.32-0.38 kWh/Nm³ (at 93% purity).
  • Saves 30% more electricity than traditional PSA and 50% more than cryogenic method.

Intelligent Control System

  • Equipped with adaptive optimization algorithm to automatically track load changes.
  • Closed-loop purity control with fluctuation range < ±0.5%.

Long-Service-Life Design

  • Molecular sieve wear resistance > 98% with service life ≥ 8 years.
  • Valve cycle life > 3 million times with annual failure rate < 0.5%.

Modular Architecture

  • Standard modules: 50/100/200 Nm³/h, parallel connection up to 6000 Nm³/h.
  • Installation cycle is 60% shorter than traditional equipment.

V. Reflection of Technical Strength

Application of Innovative Technologies

  • Isothermal adsorption model predictive control technology.
  • Four-tower rapid switching process (cycle 90-120 seconds).
  • Heat-coupled vacuum cooling system.

Performance Guarantee System

  • Molecular sieve packing density control accuracy ±1.5%.
  • Gas flow distribution uniformity deviation < 5%.
  • Online purity analyzer accuracy: Class 0.1.

VI. Product Series Introduction

Standard Model Configuration

  • VPSA-50 Series: 50-500 Nm³/h (basic industrial use)
  • VPSA-100 Series: 500-2000 Nm³/h (metallurgy, chemical industry)
  • VPSA-200 Series: 2000-6000 Nm³/h (large-scale projects)

Special Customized Models

  • Explosion-proof type (Ex d Ⅱ CT4)
  • High-altitude type (effective at 3000 meters above sea level)
  • Container type (all-weather protection class IP55)

VII. Application Scenario Solutions

Customized Solutions for Metallurgical Industry

  • Electric furnace steelmaking: 93% purity, 0.8 MPa pressure.
  • Blast furnace oxygen enrichment: 70-80% purity, large-flow continuous oxygen supply.

Applications in Environmental Protection Field

  • Sewage treatment: Oxygen utilization rate increased to 35-40%.
  • Waste incineration: Combustion-supporting oxygen reduced by 20%, flue gas emissions reduced by 30%.

Medical and Health Configuration

  • Medical oxygen standard (GB 8982-2009)
  • Dual-unit redundant backup with online switching < 3 seconds.

VIII. Detailed Technical Indicators

Performance Parameters

Parameter ItemTechnical Indicators / Description
Output Range5-6000 Nm³/h (supports modular expansion)
Oxygen Purity70%-94% (adjustable online)
Outlet PressureVPSA direct output ≤ 20 kPa; after pressurization ≤ 0.8 MPa
Dew Point Temperature≤ -60℃ (atmospheric pressure)

Energy Efficiency Indicators

Parameter ItemTechnical Indicators / Description
Specific Power Consumption0.32-0.45 kWh/Nm³ (varies with purity)
Cooling Water Consumption≤ 0.5 m³/h (water-cooled type only)
Noise Level≤ 82 dB(A)

Reliability Indicators

Parameter ItemTechnical Indicators / Description
Continuous Operation Time≥ 8000 hours
Automatic Control Rate100%
Load Regulation Range30-110%