Large-scale Air Separation Unit for Steel Mill

Large-scale Air Separation Unit for Steel Mill

Large-scale Air Separation Units for Steel Mills provide continuous, high-purity oxygen, nitrogen, and argon directly to Blast Furnaces, BOFs, EAFs, and DRI plants. Engineered for 24/7 non-stop operation, these systems integrate cryogenic distillation, process automation, and optimized refrigeration to ensure a reliable gas supply for modern steelmaking operations.
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Product Overview

 

Large-scale Air Separation Units for Steel Mills provide continuous, high-purity oxygen, nitrogen, and argon directly to Blast Furnaces, BOFs, EAFs, and DRI plants. Engineered for 24/7 non-stop operation, these systems integrate cryogenic distillation, process automation, and optimized refrigeration to ensure a reliable gas supply for modern steelmaking operations.

 

Industry-Specific Advantages

 

Uninterrupted High-Volume Supply: Built for multi-year continuous operation, supporting heavy steelmaking loads with zero unscheduled down-time.

 

Metallurgical Oxygen Purity: Delivers oxygen at ≥ 99.6% purity, meeting exact standards for BF enrichment, BOF decarburization, and EAF burner injection.

 

Wide-Range Load Turndown: Smoothly adapts gas output from 50% to 105% capacity to match variable steel mill production schedules without dropping product purity.

 

Multi-Gas Revenue Maximization: Simultaneously captures high-purity nitrogen for inerting and liquid argon for stainless steel production, maximizing overall air utilization.

 

Applications in Steel Manufacturing

 

Blast Furnace (BF): High-volume oxygen enrichment to boost pig iron productivity and reduce coke ratios.

 

Basic Oxygen Furnace (BOF): Rapid oxygen blowing for efficient carbon removal and melt refining.

 

Electric Arc Furnace (EAF): Chemical energy assistance via oxygen-fuel burners and lancing.

 

Direct Reduced Iron (DRI): Reformer gas synthesis and process gas cooling/protection.

 

Continuous Casting & Processing: High-purity nitrogen for molten steel shielding and cutting operations.

 

Parameter

 

Oxygen

Output

Purity

Pressure

Single set 20000-100000+Nm ³/h

≥ 99.6%

Oxygen consumption for blast furnace:~0.8-1.6 MPa

Oxygen for converter: 2.5-3.5 MPa

 

Nitrogen

Output

Purity

Pressure

About 2-3 times the oxygen production

99.999% (≤ 10 ppm O₂)

Multiple types: from low-pressure blowing to medium pressure spraying.

 

Argon

Output

Purity

Approximately 5% -12% of oxygen production

≥ 99.999%

 

Operation and energy consumption

Unit oxygen consumption

Annual operating time

0.35 – 0.45 kWh/Nm³ O₂

≥ 8,300 hours

(For reference only)

 

Engineering & Customization Scope

 

We customize each cryogenic system according to local plant utilities and operational targets:

Design Parameter

Customization Scope

Oxygen Capacity

Engineered to project requirements (Nm³/h)

Delivery Pressure

Customized per furnace injection specs (BarG)

System Configuration

Double-column / Single-column / Argon recovery

Automation Architecture

Siemens / ABB / Honeywell PLC & DCS Systems

Electrical & Safety

IEC / ANSI / NEC / ATEX compliant design

Compressor Selection

Centrifugal air / booster compressor matching

Site Adaptation

Extreme climate, altitude, and utility-water design

 

Project Execution & Delivery

 

Technical Consultation: Gas demand analysis and energy optimization study.

 

Process Engineering: PFD, P&ID, HAZOP analysis, and 3D layout modeling.

 

Manufacturing: In-house fabrication of heat exchangers, cold box, and pressure vessels.

 

Pre-Shipment Testing: FAT inspection, instrument calibration, and packing validation.

 

Site Execution: Turnkey supervision, cold-box perlite filling, and pipe integration.

 

Commissioning & Training: System cooldown, performance test run, and site crew safety training.

 

Engineering Support & After-Sales

 

On-site installation supervision and commissioning management.

 

24/7 remote diagnostics and process optimization assistance.

 

Original spare parts management and preventative maintenance programs.

 

Field operator training covering regular operation, safety protocols, and emergency procedures.

 

FAQ

 

Q: How does the ASU respond to sudden oxygen demand fluctuations in the steel mill?

A: The automated control system monitors pipeline pressure in real time and automatically regulates compressor guide vanes and column valves. This enables smooth load adjustments between 50% and 105% of rated capacity while maintaining steady purity.

Q: Can a liquid storage backup system be integrated into the ASU design?

A: Yes. We integrate liquid oxygen (LOX) and liquid nitrogen (LIN) storage tanks with automated ambient vaporizers to provide seamless standby gas supply during power outages or ASU maintenance.

Q: What critical utilities must the steel mill provide for site installation?

A: The site must provide primary electrical power, cooling water circulation, instrument air, and a level foundation. Exact electrical load and water consumption figures are defined during the preliminary engineering phase.

Q: Is it possible to connect the new ASU to our existing mill gas piping and DCS?

A: Yes. Our automation team custom-designs communication interfaces (Modbus, Profibus, Ethernet/IP) to link seamlessly into your centralized plant DCS and existing gas distribution networks.

Q: What international design codes and manufacturing standards can you comply with?

A: Equipment can be designed and certified according to ASME, CE/PED, GB, ISO, IEC, and local safety standards based on the final project destination.

Q: What technical supervision is provided during installation and commissioning?

A: We dispatch certified mechanical, electrical, and cryogenic process engineers to supervise site assembly, cold box perlite filling, system cooldown, and initial performance run until stable gas output is achieved.

Q: What key factors determine the overall CAPEX and OPEX of a steel mill ASU?

A: CAPEX is governed by required oxygen capacity, argon recovery inclusion, and backup storage size. OPEX is primarily driven by local power costs, compressor energy efficiency, and cooling water temperatures.

 

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