Cryogenic ASU Pre Purification Package
Front end TSA pre purification package for cryogenic air separation units removing water, carbon dioxide, and trace hydrocarbons before the cold box.
A Cryogenic ASU Pre Purification Package removes water, carbon dioxide, and trace hydrocarbons from the air feed to a cryogenic air separation unit. Twin or triple TSA adsorbers charged with 13X molecular sieve hold outlet water below 0.1 ppmv and outlet carbon dioxide below 1.0 ppmv to protect the cold box main exchanger and the distillation column.
Cold Box Protection on a Graded Adsorbent Bed
The SorbiTech Cryogenic ASU Pre Purification Package sits at the front end of every cryogenic air separation plant, removing the contaminants that would freeze and accumulate in the cold box. Without effective pre purification, the cold box main heat exchanger blocks within months and the operator faces a costly defrost campaign. The package uses a graded bed: an inlet layer of activated alumina drying grade for bulk water removal at near isothermal conditions, then the main bed of SorbiTech 13X molecular sieve for residual water, carbon dioxide, and trace hydrocarbon capture.
TSA Cycle With Waste Nitrogen Regeneration
The standard cycle is temperature swing with regeneration on dry waste nitrogen returned from the cold box. The waste nitrogen is heated to 180 to 250 °C, passed through the off line vessel in counter flow, and vented after recovering the captured water and carbon dioxide. The integration with the ASU heat recovery loop makes the parasitic energy of the pre purification a fraction of the total plant energy.
Scope of Supply
The complete package includes:
- Twin or triple adsorber vessels to ASME VIII or PED
- Layered charge: alumina inlet (SorbiTech drying grade) plus 13X main bed (SorbiTech 13X)
- Regeneration gas heater integrated with the cold box waste nitrogen loop
- Switching valve manifold rated for the ASU cycle frequency
- PLC or DCS sequence control with full cold box integration
- ATEX or IECEx zone certification per project
Defrost Interval and Operator Economics
A correctly sized pre purification bed extends the campaign between defrosts from 1 to 3 years (typical for a poorly engineered front end) to 4 to 7 years (typical for a well engineered SorbiTech package). The reduction in defrost frequency is the single largest operating saving available to an ASU owner, recovering several hundred thousand euros per year on a mid scale plant. SorbiTech sizes the bed for the operator target defrost interval and the contracted cold box specification.
Delivery
Delivered turnkey by SorbiTech or fabricated to client drawings under SorbiTech scope, with full integration with the ASU process licensor (Air Liquide, Linde, Air Products, Praxair design standards). Sector coverage is industrial gas and air separation.
Engineered Scope
Project References
Applications This System Serves
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01
Process Duty
Beverage Carbon Dioxide Purification
Pellet activated carbon guard bed for beverage grade carbon dioxide purification meeting ISBT (International Society of Beverage Technologists) specifications for carbonated soft drinks, beer,…
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02
Process Duty
Solvent Vapor Recovery
Solvent vapor recovery using twin tower pellet activated carbon adsorbers with steam or vacuum regeneration to capture and recover volatile organic solvents from process…
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03
Process Duty
LPG and Propane Drying and Treating
Drying and sulphur removal from liquefied petroleum gas (LPG), propane, and butane streams using 3A molecular sieve and impregnated activated carbon to meet pipeline…
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04
Process Duty
Oxygen Generation (PSA / VSA)
On site oxygen generation by pressure swing or vacuum pressure swing adsorption using lithium exchanged X zeolite for medical, aquaculture, ozone, and metals applications.
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05
Process Duty
Cryogenic ASU Air Pre Purification
Pre purifying air feed to cryogenic air separation units by removing water, carbon dioxide, and trace hydrocarbons on a graded molecular sieve and activated…
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06
Process Duty
Instrument and Plant Air Drying
Heatless desiccant drying of compressed instrument air and plant air using activated alumina to deliver pressure dew points below minus 40 °C for DCS…
Media Used in This System
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01
Adsorbent
Activated Alumina Drying Grade
High capacity activated alumina for compressed air dryers, gas dehydration, and heatless desiccant systems.
Water Cap.
≥ 20 %
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02
Adsorbent
Molecular Sieve 13X
Sodium form 13X zeolite for cryogenic air pre purification and combined drying and sweetening.
Pore Ø
10 Å
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03
Adsorbent
Carbon Molecular Sieve CMS 450HP
Ultra high purity carbon molecular sieve. 99.99999 percent (7N) N2, selective O2 and CO2 capture, 1.0 to 1.6 mm pellets, minimal fines, deoxo polishing…
Water Cap.
Feed must reach ISO 8573 class 1.4.1, deoxo polishing recommended for 7N %
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04
Adsorbent
Carbon Molecular Sieve CMS 420KT
High efficiency carbon molecular sieve. Higher oxygen affinity under 7 to 12 barg, 1.2 to 1.8 mm pellets, Snowstorm Filling compatible, ASTM D4058 attrition…
Water Cap.
Feed must reach ISO 8573 class 1.4.1 %
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05
Adsorbent
Carbon Molecular Sieve CMS 350KT
Rapid adsorption carbon molecular sieve. 40 to 90 second cycle at 7 to 10 barg, up to 99.99 percent N2, 1.0 to 2.2 mm…
Water Cap.
Moisture at supply below 1.0 percent, feed must reach ISO 8573 class 1.4.1 %
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06
Adsorbent
Activated Alumina Impregnated
Promoter loaded activated alumina for hydrogen sulphide, chloride, and Claus tail gas guard duty.
Form
3–5 mm spheres · 1.6–3.2 mm spheres
Discuss Your Engineering Requirements
Our engineers review your duty conditions and recommend the right configuration.