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Stripper Column

Stripper Columns

Leading Manufacturer of Stripper Columns

Stripper Columns

We offer a wide range of columns to meet the needs of a variety of applications. Our columns are designed and manufactured to the highest standards, and we offer a comprehensive range of services, including engineering, construction, and start-up support.

When designing an effluent stripper column, the choice between structured packing and sieve trays can significantly impact the efficiency, operational flexibility, and overall performance of the system. Here's a comparison to help you decide which might be more suitable for your specific needs:

Efficiency and Performance Of Structured Packing Over Sieve Trays

Structured Packing

  • High Surface Area

  • Low Pressure Drop

  • Higher Mass Transfer Efficiency

  • Low Space Efficiency

  • Higher Design Flexibility

  • Wide range of Turn Down Ratio

  • Less Maintenance

  • Low Initial Cost

  • Low Operational Costs

Sieve Tray

  • Low Surface Area

  • Higher Pressure Drop

  • Low Mass Transfer Efficiency

  • High Space Efficiency

  • Lower Design Flexibility

  • Less Turn Down Ratio

  • High Maintenance

  • High Initial Cost

  • High Operational Costs

Effluent stripper process flow diagram

Summary

  • Structured Packing: Offers higher efficiency, lower pressure drop, and better operational flexibility but comes with a higher initial cost. Ideal for applications where space is limited and energy efficiency is crucial.

  • Sieve Trays: Provide a robust and cost-effective solution with easier maintenance and handling of high flow rates but at the expense of higher pressure drops and potentially lower efficiency. Suitable for large-scale operations where cost and durability are major concerns.

Ultimately, the choice depends on your specific application requirements, budget constraints, and operational goals.

FAQs

It is a flat perforated plate with no moving parts & made up of simply metal with holes in them. Vapour passes straight upward through the liquid on the plate. The arrangement, number, and size of the holes are design parameters.

Sieve trays are typically fabricated from sheet metal — commonly stainless steel or other corrosion-resistant alloys selected to suit the process fluid — with a regular pattern of small holes punched or drilled across the active area.

Vapour rising through the perforations contacts the liquid flowing across the tray, creating a froth that promotes mass transfer. The vapour velocity must be high enough to stop liquid weeping through the holes, yet low enough to avoid excessive entrainment and flooding.

Hole sizes typically range from about 3 mm to 12 mm, with the open area generally between 6% and 15% of the active tray area. The exact geometry is set during design to balance capacity, efficiency, and turndown for the specific service.

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