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Chemical plant heat exchanger cleaning

The deposit in a chemical plant exchanger is whatever that process makes, usually concentrated and often changed. Send the unit details, the service and what you know about the residue, and a specialist set up for that chemistry will come back to you.

  • UnitsReactor coolers, condensers, interchangers, graphite
  • DepositsPolymer, salts, catalyst fines, thermal fluid coke
  • Starts withIdentifying the deposit

Submit a cleaning request

Four steps: unit, deposit, postcode, contact details.

  1. 01Unit
  2. 02Situation
  3. 03Site
  4. 04Contact
What needs cleaning?

01What gets cleaned

Reactor service, vent condensers and thermal fluid systems foul from three different causes

Chemical plant heat exchanger cleaning is the one sector where the deposit cannot be assumed. A reactor cooler on one plant is fouled with polymer that dissolves in a specific solvent and nothing else; the same unit on the next plant carries crystallised salt that water removes in an hour. Quoting a method before the residue is identified is guesswork, and on reactive or unstable residues it is worse than guesswork.

01

Reactor coolers and interchangers foul with the reaction and not with the feed

Anything that removes heat from a reaction sees the product, the by-products and whatever polymerises at the wall. Monomer service is the clearest case: styrene, acrylate and vinyl streams polymerise on hot surfaces, and once a film has formed it insulates, raises wall temperature and accelerates the next layer. Inhibitor systems are designed to hold this off, and fouling that starts suddenly is often an inhibitor problem rather than a cleaning problem.

Fouls with
Polymer and popcorn polymer, oligomers, tars, reaction by-products
First symptom
Cooling duty falling, reaction temperature harder to hold, pressure drop up
Watch for
Inhibitor depletion upstream, which will refoul a cleaned unit quickly
02

Graphite and exotic alloy units limit what chemistry can be used at all

Halogen acid service means graphite block and shell-and-tube graphite exchangers, and those tolerate acids that would destroy stainless while being mechanically fragile and impossible to lance the way a metal bundle can be. Hastelloy, titanium, zirconium and glass-lined equipment each have their own compatibility windows. Here the material decides the method before the deposit gets a say, and a chemistry chosen on the deposit alone has written off exchangers before now.

Fouls with
Salts, iron chlorides, process solids, polymer
First symptom
Duty loss, and pluggage, not gradual coating
Watch for
Block cracking under jetting pressure, cement joint attack, thermal shock
03

Thermal fluid heaters coke from the inside when the oil degrades

Hot oil systems degrade with time and temperature, and the degradation products lay down carbon on the hottest surfaces. Heater tubes and user exchangers. The classic sequence is a film forming, wall temperature rising because of it, and the higher wall temperature degrading more oil. Cleaning the exchanger without sampling the fluid treats the symptom: if the oil is out of specification, the same deposit is back inside a year.

Fouls with
Carbon, sludge and degraded thermal fluid, plus scale on the process side
First symptom
Users not reaching temperature, heater skin temperatures rising
Watch for
Fluid analysis out of specification, which is the actual root cause

02What has built up

The residue is often more concentrated and more reactive than the process stream

A deposit is what came out of solution and stayed. That makes it a concentrate, and concentrates behave differently from the streams they came from. Including on the safety data sheet.

DepositWhere it comes fromHow it is removed
PolymerMonomer and reactive streams polymerising at the hot wall, particularly where inhibitor has been depleted.Solvent circulation matched to the specific polymer, or jetting once it has cross-linked.
Solvent / UHP
Crystallised saltsStreams cooled past a solubility limit, or carried past a point where two streams meet and precipitate.Warm water or dilute acid circulation. Frequently the easiest deposit in the sector to remove.
CIP
Catalyst finesAttrition carrying fines downstream, settling in shell bottoms, baffle windows and low-velocity areas.Back-flushing and jetting. They were never dissolved, so nothing dissolves them out.
UHP / back-flush
Thermal fluid cokeHot oil degrading at the wall in heater and user exchangers, laying down carbon that insulates.Solvent flush while soft, jetting once hard. Fluid condition has to be corrected or it returns.
Solvent / UHP
Iron chlorides and corrosion productsHalogen acid service, and any wet acidic duty attacking upstream carbon steel.Chelant or inhibited acid, chosen against the exchanger material instead of the deposit.
CIP
Unknown residueMulti-product plant, campaign changes, or a unit that has not been opened in a decade.Sample and identify first. Everything else follows from that and nothing sensible precedes it.
Identify first

03In place or off site

The deposit is identified before a chemistry is chosen, not after

This is the sector where the order of operations matters most. A cleaning agent selected on a guess can react with the residue, attack the exchanger material, or produce a waste stream the site cannot legally take.

  1. 01

    Sampling the deposit is the first activity and it changes the whole job

    A physical sample, analysed for composition and solubility, converts guesswork into a method. It also flags reactivity and any hazard that has concentrated in the residue. On a unit with unknown history this is the difference between a fixed price and a day rate.

  2. 02

    Material compatibility rules out chemistry before the deposit narrows it down

    Graphite, glass lining, titanium, zirconium and the exotic nickel alloys each rule out particular acids, particular temperatures and particular chloride levels. The compatibility check comes first and is non-negotiable, because getting it wrong destroys equipment with lead times measured in months.

  3. 03

    Decontamination makes the unit safe to open where the residue is the hazard

    Where the exchanger has held toxic, pyrophoric or reactive material, chemical or vapour-phase treatment removes and neutralises the residue before anyone breaks a flange. It is planned as a separate step from cleaning because it answers a different question.

  4. 04

    Jetting under containment handles everything that was never in solution

    Catalyst fines, cross-linked polymer and set solids come out mechanically. The work is done inside a bunded bay or containment so the effluent is captured, characterised and disposed of under duty of care instead of reaching a site drain.

04What happens next

Four steps take a fouled unit from enquiry to a tested return

The enquiry goes straight to a contractor who cleans that unit type. There is no qualifying call in between.

  1. You send the unit details, the deposit and the postcode.

  2. The enquiry goes to a specialist set up for that unit type and that fouling.

  3. They come back with method, timescale and price.

  4. The clean is carried out in place or off site, and the unit is tested before it goes back.

05Questions

Deposit identification, material compatibility and waste routing decide how chemical plant is cleaned

We do not know what the deposit is. Can it still be cleaned?

Yes, and this is the normal starting position and not an unusual one. What it changes is the sequence: a sample is taken and analysed for composition and solubility before a method is proposed, and that analysis is what makes a fixed price possible.

Be wary of a method quoted confidently against an unidentified residue. On a chemical plant that is either a guess or an assumption that the deposit matches something the contractor has seen before, and both have gone wrong expensively.

Can the deposit be more hazardous than the process fluid?

Frequently, and it is the thing most often underestimated. A deposit is material that came out of the stream and stayed, so it is a concentrate. Heavy metals, catalyst residues and reaction by-products all concentrate this way.

It can also be a different substance entirely. Degradation and reaction in place mean the residue may not appear on the safety data sheet for the process stream at all, which is another reason the sample matters before the method.

How are graphite block exchangers cleaned?

Carefully, and rarely with high pressure. Graphite tolerates hydrochloric and sulphuric service that would destroy stainless, so it is there, but it is mechanically brittle and the cement joints are vulnerable to both pressure and thermal shock.

Chemical circulation at controlled temperature is the normal route, with mechanical cleaning limited to low-pressure lancing and rodding within the manufacturer's limits. Thermal shock does as much damage as over-pressure, so heating and cooling rates matter as much as the chemistry.

Our thermal fluid system keeps coking. Will cleaning fix it?

Cleaning fixes the exchanger. It does not fix the reason the exchanger fouled, and on a hot oil system that reason is usually the fluid itself.

Degraded thermal fluid lays down carbon, the carbon raises wall temperature, and the higher wall temperature degrades more fluid. Unless fluid condition is sampled and corrected, or the system is flushed and recharged, a cleaned heater will foul again on the same curve. Clean and analyse together, not one or the other.

Can polymer fouling be dissolved rather than jetted?

It depends entirely on whether it has cross-linked. Linear polymer and oligomer often dissolve readily in a solvent matched to that specific polymer, which is the cheap and quick outcome.

Cross-linked and popcorn polymer does not dissolve in anything practical, and it comes out mechanically. Which one is present is a question for the sample, not for the process description, because the same unit can carry both in different places.

What happens to the cleaning waste?

It is characterised and disposed of under duty of care, and on this plant it is often the most constrained part of the job. Spent chemistry carrying concentrated process residue can be a more difficult waste than anything the site normally consigns.

Raising is early. Some sites have their own effluent route that can take it, some cannot, and the disposal route can change the choice of cleaning method. Occasionally making jetting preferable because it produces no spent chemical stream.

What does chemical plant exchanger cleaning cost?

It is the sector with the widest range, and the spread is driven by the deposit instead of by the unit. Crystallised salt washed out with warm water and cross-linked polymer removed from a Hastelloy bundle are barely the same activity.

Sampling first is what narrows it. A quote against an identified deposit is a price; a quote against an unidentified one is a day rate with an open end, and the sample usually costs less than the difference.

How often should these exchangers be cleaned?

By trended performance, and then by turnaround availability. Heat transfer against clean-condition baseline is the measurement that says when a unit has stopped earning its place.

The more useful question in this sector is usually why the fouling rate has changed. A unit that suddenly fouls faster is telling you something upstream has moved, inhibitor, catalyst attrition, feed composition or fluid condition, and cleaning it on a shorter cycle treats the symptom.

A specialist who cleans that unit type answers the request

Unit, deposit and postcode are enough to start. Your details go to a specialist who cleans that unit type. No obligation.