Pingxiang Daier Separation Tech Sep 9, 2026

Structured Packing for 1,4-Butanediol Purification: Vacuum Distillation, THF Formation and Side-Draw Product Recovery

Structured Packing for 1,4-Butanediol Purification: Vacuum Distillation, THF Formation and Side-Draw Product Recovery

Purifying 1,4-butanediol is not simply a high-boiling distillation problem.

BDO has a high normal boiling point, and prolonged exposure to elevated temperature can promote unwanted side reactions. One important consequence is the formation of tetrahydrofuran and water from 1,4-butanediol under unfavorable thermal conditions.

At the same time, crude BDO can contain water and lower-boiling components above the desired product range, while organic tars, salts and higher-boiling glycols or diols remain below it.

That creates an attractive separation structure:

water and light impurities overhead → high-purity BDO in the middle → heavy impurities in the bottoms.

Structured packing is well suited to this duty because a high number of effective stages can be installed with relatively low pressure drop and liquid holdup, helping the column operate under deep vacuum without unnecessarily increasing the temperature of the product.

Why BDO Purification Needs Vacuum

1,4-Butanediol is substantially less volatile than many common organic solvents.

Trying to purify it at high absolute pressure pushes the required boiling temperature upward.

That creates two problems.

The first is straightforward: higher temperature means higher thermal duty.

The second is more important for product quality: BDO can undergo thermal degradation or dehydration.

An early industrial purification process specifically noted that heating crude 1,4-butanediol can generate water and tetrahydrofuran, and therefore operated the distillation column below about 200 mmHg absolute to reduce the required temperature.

Later process development likewise operated the BDO purification column under vacuum while keeping reboiler temperature below roughly 175°C.

Modern BDO purification remains strongly connected to vacuum operation because the system contains high-boiling and temperature-sensitive components. A 2025 process study again identifies vacuum distillation as the preferred industrially mature method for high-boiling BDO mixtures because it lowers separation temperature.

For structured packing, this makes pressure drop a process variable—not just a hydraulic specification.

Every Pressure Drop Raises the Bottom Temperature

Suppose the top of a BDO finishing column operates at only a few kilopascals absolute.

The bottom does not operate at exactly the same pressure.

As vapor passes through the packing, distributors, collectors and other internals, pressure gradually increases downward.

The relationship is simple:

bottom pressure = top pressure + total internal pressure drop

If total ΔP becomes large, the reboiler has to operate at a higher temperature.

That partly defeats the reason the vacuum system was installed.

A recent BDO purification patent gives a particularly clear industrial example: the finished-product column uses Sulzer BXPlus packing, operates at approximately 3 ± 0.5 kPa absolute, and runs near 160°C. Separate BDO light-component and heavy-component recovery towers also use BXPlus packed beds under very low absolute pressures.

That makes low-pressure-drop structured packing especially valuable.

The packing is helping preserve the low-temperature operating window of the complete tower.

THF in a BDO Column Can Be a Sign of Thermal History

Tetrahydrofuran has an interesting relationship with BDO.

THF can be deliberately produced from 1,4-butanediol by dehydration.

In a BDO purification column, however, formation of additional THF can represent unwanted product loss.

Historical BDO purification technology specifically notes that THF formed from BDO decomposition leaves with the lighter overhead material.

So if THF concentration in the overhead increases unexpectedly, the plant should not immediately treat that only as a light-end separation problem.

It may also be worth asking whether:

  • reboiler temperature has increased;
  • vacuum performance has deteriorated;
  • residence time has increased;
  • heavy material is fouling heat-transfer surfaces;
  • column pressure drop has increased.

In other words, more THF may sometimes be telling the plant something about the thermal condition of the BDO purification system.

That is a much more specific engineering question than generic “vacuum distillation efficiency.”

Water and Light Components Belong Above the Product

Crude BDO can contain water together with compounds boiling below BDO.

In one classic purification design, crude feed contained roughly 1–20% water, with lower-boiling organic impurities and smaller amounts of heavy organic tars and inorganic salts.

The column sends water and light material toward the overhead.

This makes the upper packed section mainly responsible for preventing those components from contaminating the BDO product.

If the upper bed loses effective separation because of poor liquid distribution, possible symptoms include:

  • higher product water;
  • increased THF or light impurities in BDO;
  • need for higher reflux;
  • reduced throughput at the same specification.

Therefore, a product-water problem should not automatically trigger replacement of the whole column packing.

The upper distributor and upper packed bed may deserve the first inspection.

Heavy Tars and Salts Belong Below the Product

The opposite problem exists at the bottom.

Crude BDO may contain:

  • high-boiling organic material;
  • heavier diols;
  • color-forming compounds;
  • inorganic salts;
  • tars.

The purpose of the lower separation is to prevent those materials from travelling into the purified BDO stream.

Recent BDO research highlights difficult high-boiling impurity systems involving ethylene glycol, 3-methyl-1,5-pentanediol and 1,6-hexanediol.

This creates an important packing-design issue.

The bottom section is typically less clean than the top.

As heavies become concentrated, liquid viscosity and deposit tendency may increase.

A very fine packing may provide excellent theoretical-stage efficiency in a clean simulation but offer less margin if salts or tar reach the bed.

The lowest packed section therefore should not automatically receive the finest geometry available.

Long-term cleanliness matters.

Why the Purest BDO May Be Taken From the Middle

BDO purification is another useful example where the finished product does not necessarily come from the top or bottom of the column.

If the column establishes the correct composition profile:

water / THF / lightsmove upward,

heavy diols / tar / saltsmove downward,

and a zone of maximum BDO purity develops between them.

Historical BDO purification technology therefore withdrew substantially pure 1,4-butanediol from a side location rather than taking the main product directly from an endpoint.

Newer bio-based BDO purification technology follows the same general concept: low boilers are first removed, high boilers are then rejected, and purified BDO can be collected through a side draw from the purification column.

This is particularly relevant to a structured packing retrofit.

The product nozzle is physically fixed.

But its theoretical-stage position depends on packing efficiency.

If the old packing is replaced with a substantially different HETP, the best composition zone may shift even though the nozzle does not.

Therefore, an “upgrade” to more efficient packing can require a process re-rating rather than simple mechanical replacement.

The Side Draw Makes Bed Arrangement Important

A side-draw BDO product column may require separate structured packing beds rather than one uninterrupted packing block.

A typical arrangement can be:

upper packed bed→ liquid collector→ BDO side draw→ redistributor→ lower packed bed

The upper section rejects water and light impurities.

The lower section rejects heavies.

The collector establishes the liquid available at the product withdrawal point.

The remaining liquid must then be evenly redistributed below.

If the collector or redistributor performs poorly, one part of the column can appear healthy while the other loses efficiency.

For a BDO replacement project, the packing volume alone is therefore insufficient.

DAIER should ideally receive:

  • tower elevation drawing;
  • feed elevation;
  • product side-draw elevation;
  • bed heights;
  • collector arrangement;
  • distributor arrangement;
  • support-grid elevations.

These determine how the packing participates in the actual separation.

Modern BDO Plants Use High-Efficiency Structured Packing Directly

There is strong recent evidence that high-efficiency structured packing is not merely a theoretical option in this duty.

A recent industrial purification disclosure specifies:

  • finished-product column: Sulzer BXPlus packed tower;
  • approximately 3 kPaA operating pressure;
  • two packed sections;
  • high reflux ratio;

and separately uses BXPlus structured packing in both the BDO light-component recovery and heavy-component recovery columns.

Earlier industrial designs also identified Koch/Sulzer-type mesh packing as a suitable column internal in BDO vacuum purification.

This tells us where high-efficiency structured packing has the strongest value:

cleaner BDO finishing and recovery sections that need many theoretical stages under very low pressure.

It does not mean every dirty upstream BDO stream should receive fine gauze packing.

Stream cleanliness still matters.

New BDO Routes Change the Impurity List

Traditional BDO has been produced through routes such as the Reppe process.

New bio-based processes can produce 1,4-BDO from fermentation broth.

These routes do not necessarily generate the same contaminants.

Bio-based purification schemes may need to remove:

  • salts;
  • water;
  • fermentation-derived compounds;
  • lower-boiling organics;
  • higher-boiling materials.

The relevant technology explicitly allows distillation columns containing structured packing, random packing, trays or combinations of these internals.

That means an RFQ saying:

“1,4-BDO purification, 99.9% product”

still does not fully define the packing duty.

The supplier needs to know where the crude BDO came from.

The feed impurity profile determines whether the packed section is a clean finishing service or a contamination-prone recovery service.

Energy Reduction Is Becoming Part of BDO Column Design

Vacuum distillation solves the high-temperature problem but BDO purification can still consume substantial energy.

The separation involves high-boiling compounds and often several columns.

Recent research therefore evaluates:

  • heat-pump distillation;
  • dividing-wall columns;
  • integrated separation configurations.

A 2025 study specifically compares conventional BDO purification with heat-pump and dividing-wall alternatives to reduce energy consumption while maintaining difficult high-boiling impurity separations.

Structured packing can support these designs because lower pressure drop and high stage density reduce the hydraulic penalty of putting more separation duty into a compact column.

But the packing alone does not produce the energy savings.

The benefit depends on integration with:

  • condenser;
  • reboiler;
  • vacuum system;
  • heat pump;
  • feed condition;
  • recycle streams.

A revamp should therefore be evaluated as a complete separation system.

What DAIER Needs for a BDO Purification RFQ

The first question should identify the exact section:

  • water / light-ends removal;
  • BDO finished-product column;
  • light-component recovery;
  • heavy-component recovery;
  • bio-based BDO purification;
  • integrated or dividing-wall column.

The design basis should then include:

  • BDO concentration;
  • water content;
  • THF;
  • methanol or other light compounds;
  • ethylene glycol;
  • other diols;
  • heavy organic impurities;
  • salts or solids;
  • required BDO purity;
  • allowable water;
  • individual impurity limits;
  • operating pressure;
  • top and bottom temperature;
  • reflux ratio;
  • vapor and liquid rates;
  • tower inside diameter;
  • packed height by bed;
  • feed elevation;
  • product side-draw elevation;
  • allowable pressure drop;
  • current packing;
  • distributor and collector arrangement;
  • fouling history.

For a retrofit, three operating trends are especially useful:

vacuum pressure + bottom temperature + THF concentration.

Together they can help show whether the column problem is only separation efficiency or whether thermal degradation is also increasing.

BDO Packing Should Protect the Product From Heat

The central engineering problem in 1,4-butanediol purification is not simply obtaining a low HETP.

The column must place three groups of material in different directions:

water and light compounds upward,pure BDO into the product zone,heavy impurities downward.

It must do this while keeping operating temperature low enough to avoid unnecessary BDO degradation.

That is why structured packing fits the service so well.

It can provide:

high stage density + low pressure drop + low liquid inventory + side-draw flexibility.

The useful selection question is therefore:

Which structured packing can provide enough effective stages above and below the BDO product zone while keeping total vacuum-column pressure drop low enough to limit BDO-to-THF thermal degradation?

That is the application-specific engineering value of structured packing in BDO purification.

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