Pingxiang Daier Separation Tech Aug 19, 2026

Tower Packing Selection When Tower Diameter Is Not Yet Known

Tower Packing Selection When Tower Diameter Is Not Yet Known

A common situation in a new packed tower project is:

We know the process conditions, but the tower diameter has not been decided yet. Can we still start selecting tower packing?

Yes—but only at a preliminary screening level.

When tower diameter is not yet known, the DAIER Tower Packing Engineering Assistant can still help organize the project, screen preliminary packing directions and identify the information required for the next engineering stage.

However, some calculations cannot yet be completed.

The key is to separate:

what can be screened now

from

what must wait until tower geometry is confirmed.

[Use the DAIER Tower Packing Engineering Assistant → https://www.pxdaier.com/tower-packing-engineering-assistant.html]


The Short Answer

If tower diameter is not yet known, you can still review:

process application

gas and liquid conditions

operating temperature

operating pressure

process media

corrosion conditions

fouling tendency

preliminary material family

preliminary packing structure

project priorities

But you cannot yet reliably confirm:

packing volume

total packing quantity

packing weight

packing-to-column size relationship

superficial gas velocity based on actual tower area

final packing size

final hydraulic capacity

This is why a new tower project should not stop just because the vessel diameter is still under development.

The project can still move forward—just at the correct level of engineering certainty.


1. Start with the Process, Not the Packing Size

When tower diameter is unknown, do not begin by asking:

Should I use 25 mm or 50 mm packing?

That question comes too early.

Start with the process itself.

Useful information includes:

process duty

gas flow

liquid flow

operating temperature

operating pressure

gas composition

liquid composition

corrosion conditions

fouling or solids

required process performance

allowable pressure-drop considerations

These inputs help establish what the tower needs to accomplish before the physical tower dimensions are finalized.

For a complete data checklist:

[Tower Packing Selection Parameters → https://www.pxdaier.com/tower-packing-solutions/tower-packing-selection-parameters]


2. What Can the Engineering Assistant Still Screen?

Even without a confirmed tower diameter, the tool can still support preliminary direction screening.

For example, the project may begin to evaluate:

Material Family

Should the project further investigate:

plastic

metal

ceramic

based on temperature, corrosion and process chemistry?

Packing Structure

Does the application suggest further evaluation of:

random packing

structured packing

Fouling Direction

Does the process contain:

solids

crystals

scale

sticky material

polymerizing compounds

that may make a more open packing geometry desirable?

These are useful early decisions even before tower diameter is fixed.


3. Why the Tool Should Not Force an Exact Packing Model

An early-stage project may provide:

application

flow rates

temperature

pressure

process medium

but no final tower diameter.

In this situation, automatically returning one exact packing model may imply a level of certainty that does not yet exist.

For example, a specific random packing size must eventually be reviewed against the tower diameter.

The same packing size can behave differently in:

a small-diameter column

a large industrial tower

Therefore, the correct early result may remain at:

material family

packing structure

possible product family

rather than jumping directly to one final model.


4. Why Tower Diameter Matters Later

Once tower diameter becomes available, several additional checks become possible.

Tower diameter affects:

cross-sectional area

superficial gas velocity

packing quantity

packing-size suitability

wall effects

liquid distribution

hydraulic capacity

This is why diameter eventually becomes a major selection parameter.

For the full relationship, see:

[How Tower Diameter Affects Tower Packing Selection → https://www.pxdaier.com/tower-packing-solutions/how-tower-diameter-affects-packing-selection]


5. Packing Volume Cannot Be Finalized Without Tower Diameter

Packing volume for a cylindrical bed is based on:

Tower Cross-Sectional Area × Packing Bed Height

Without tower diameter, the cross-sectional area is not yet known.

Therefore, the tool cannot produce a meaningful final packing-volume estimate until the relevant tower geometry is available.

Once diameter and packing height are confirmed, preliminary volume can be calculated.

For more information:

[What Does the DAIER Tower Packing Engineering Assistant Calculate? → https://www.pxdaier.com/tower-packing-solutions/what-does-tower-packing-engineering-assistant-calculate]


6. Packing Weight Must Also Wait

Packing weight depends on:

Packing Volume × Packing Bulk Density

If tower diameter is unknown:

packing volume is not yet confirmed

total packing weight cannot yet be confirmed

You may still compare material or packing-family directions, but the project should not treat an estimated shipping weight as final.

Weight estimation becomes more useful after:

tower diameter

bed height

packing model

bulk density

are available.


7. Do Not Guess the Tower Diameter Just to Complete the Tool

This is important.

Do not enter an invented tower diameter simply because the software contains a diameter field.

A guessed value can affect:

calculated packing volume

gas velocity interpretation

packing-size comparison

quantity

weight

and may make the final result look more precise than the project actually is.

If the tower diameter is not known, keep it identified as an unresolved engineering input.

The purpose of the tool is to structure the project—not to manufacture missing engineering data.


8. Can Gas Flow Be Used to Determine the Tower Diameter?

Gas flow is an important input, but gas flow alone does not determine the final tower diameter.

Tower sizing may also depend on:

liquid loading

gas density

liquid density

operating pressure

operating temperature

packing geometry

hydraulic capacity

allowable pressure drop

flooding margin

process design criteria

Therefore:

“Gas flow = 10,000 m³/h”

is not enough by itself to finalize a packed tower diameter.

A proper hydraulic design may be required before the equipment diameter is confirmed.


9. What About Gas Velocity?

Superficial gas velocity depends on:

Gas Volumetric Flow / Tower Cross-Sectional Area

If the tower area is unknown, actual tower gas velocity cannot yet be calculated from the final geometry.

This means early screening can recognize that gas loading is important, but it cannot complete the tower-area-dependent hydraulic interpretation.

Once diameter is confirmed, the gas-flow information becomes much more useful.


10. Can Packing Size Be Selected Before Diameter?

Only at a very preliminary level.

For random packing, packing size should eventually be checked against the tower diameter.

A project may initially identify possible size families, but final confirmation should wait until the tower geometry is available.

For example, larger packing may offer:

larger flow passages

potentially lower hydraulic resistance

greater fouling tolerance

while smaller packing may offer:

higher specific surface area

But none of these advantages should be considered independently from the actual column size.

See:

[How to Choose Tower Packing Size → https://www.pxdaier.com/tower-packing-solutions/how-to-choose-tower-packing-size]


11. What Can Be Decided Before Diameter?

A surprising amount of useful work can still be completed.

Process Duty

Define whether the tower is used for:

absorption

scrubbing

stripping

distillation

gas treatment

other gas-liquid contact service

Material Direction

Review:

chemistry

temperature

corrosion

Fouling Direction

Identify:

solids

crystallization

scale

sticky contaminants

Project Priority

Define whether the project mainly prioritizes:

low pressure drop

corrosion resistance

fouling resistance

mass-transfer performance

cost

mechanical strength

These decisions can narrow the field significantly before final tower dimensions exist.


12. Example: New Scrubber Project

Assume a new scrubber project has:

Application: Acid gas scrubbingGas Flow: AvailableLiquid Flow: AvailableTemperature: 45°CPressure: Near atmosphericProcess Medium: KnownFouling: ModerateTower Diameter: Not yet determined

The Engineering Assistant can still help organize:

process information

material direction

fouling concern

preliminary packing structure

project priority

But the result should not yet be used to finalize:

25 mm vs 50 mm packing

total packing volume

total packing weight

final hydraulic capacity

Those decisions move forward after the tower geometry is defined.


13. What Happens After Tower Diameter Is Confirmed?

Once the tower ID becomes available, return to the project and update the Engineering Assistant.

Then review:

Packing Volume

Calculate the approximate packed-bed volume.

Packing Weight

Estimate weight using the confirmed packing bulk density.

Packing Size

Check size against actual tower diameter.

Gas Velocity

Review gas flow against the available cross-sectional area.

Hydraulic Concerns

Determine whether pressure drop, capacity or flooding margin requires more detailed engineering review.

The project therefore moves from:

early screening

to

geometry-based preliminary evaluation.


14. New Tower vs Existing Tower

This is one of the biggest differences between project types.

Existing Tower

The diameter is normally fixed.

The question becomes:

What packing can work inside the existing vessel?

New Tower

Diameter may still be flexible.

The question becomes:

What preliminary packing direction fits the process, and what hydraulic design is needed before the vessel geometry is finalized?

These are different engineering workflows.

For existing towers:

[How to Use the DAIER Tower Packing Engineering Assistant for an Existing Tower Replacement → https://www.pxdaier.com/tower-packing-solutions/how-to-use-engineering-assistant-for-tower-packing-replacement]


15. What Should You Send to the Engineer or Supplier?

If tower diameter is not yet known, do not send an RFQ pretending that the packing quantity is already fixed.

Instead provide:

Known Data

process duty

gas flow

liquid flow

temperature

pressure

gas composition

liquid composition

fouling information

Unknown Data

final tower diameter

final packing height

final packing quantity

Required Support

State clearly what you need.

For example:

Tower diameter has not yet been finalized. Please review the available process conditions and provide a preliminary packing direction. Final packing size and quantity will be confirmed after tower hydraulic design.

This creates a much clearer technical discussion.

For RFQ preparation:

[How to Prepare a Tower Packing RFQ with the DAIER Engineering Assistant → https://www.pxdaier.com/tower-packing-solutions/how-to-prepare-tower-packing-rfq-with-engineering-assistant]


16. When Does Detailed Hydraulic Design Become Necessary?

The project should move beyond preliminary screening when it needs to confirm items such as:

final tower diameter

exact pressure drop

hydraulic capacity

flooding margin

required separation performance

liquid distribution

final packing size

final packing arrangement

At that stage, complete process data and packing-specific engineering calculations may be required.

The Engineering Assistant is intended to help organize and narrow the project before that stage—not replace it.


A Practical Workflow When Tower Diameter Is Unknown

Step 1 — Enter the Process Information

Start with the data already available.

Step 2 — Define the Project Priority

Corrosion, fouling, low pressure drop, efficiency, etc.

Step 3 — Screen the Preliminary Packing Direction

Identify suitable material and structure directions.

Step 4 — Identify Missing Engineering Inputs

Tower diameter becomes one of the key unresolved variables.

Step 5 — Complete Hydraulic / Process Design as Required

Establish the tower geometry.

Step 6 — Return to the Engineering Assistant

Add the confirmed tower diameter and packing height.

Step 7 — Continue Packing Comparison

Review size, quantity, weight and suitable catalog options.

Step 8 — Prepare the RFQ

Send the confirmed data and preliminary selection basis to the supplier.


The Simple Answer

Can I use the DAIER Engineering Assistant without a final tower diameter?

Yes.

Use it for early project organization and preliminary packing-direction screening.

Can it calculate final packing volume without tower diameter?

No.

The tower cross-sectional area is required.

Can I finalize random packing size without tower diameter?

Not reliably.

Packing size should eventually be checked against the actual column diameter.

Can the tool determine the final tower diameter for me?

Not as a complete hydraulic design.

Final tower sizing may require detailed process and hydraulic calculations.

Should I guess a diameter to obtain a result?

No.

Use known information, identify the missing variable and update the project once the diameter is confirmed.


Use the DAIER Tower Packing Engineering Assistant

The [DAIER Tower Packing Engineering Assistant → https://www.pxdaier.com/tower-packing-engineering-assistant.html] can still be useful before all tower dimensions are finalized.

Use it to:

organize process data

screen preliminary packing direction

review material requirements

identify fouling concerns

identify missing engineering information

prepare the project for the next design stage

Then return to the tool when the tower diameter and bed height become available.

This keeps early packing screening useful without presenting incomplete project information as a final engineering design.

Specs and test data available upon request.

Can the DAIER Tower Packing Engineering Assistant Select Tower Internals?

Automatic Mode vs Manual Mode in the DAIER Tower Packing Engineering Assistant