We care about your privacy

We use cookies to ensure the site functions properly, measure traffic, and personalize marketing only with your consent.

CASE STUDY

Real-time determination of the polycondensation endpoint of resins (UF/MUF)

In a feasibility study at a manufacturer of urea-melamine resins, we developed an inline indication of the polycondensation reaction endpoint, replacing manual viscosity measurement after the fact.
Głowica reaktora kondensacji żywic aminowych: napęd mieszadła, włazy i króćce procesowe
Industry
Production of urea-melamine resins (UF/MUF)
Scope
Inline determination of the polycondensation endpoint
Viscosity profile during a single batch of UF/MUF resinUp to the 43rd minute, the increase is slow and predictable. Thereafter, the rate rises several dozen-fold, and it is precisely within this window that the decision to terminate the reaction is made.
Lepkość w czasie szarży: wolny przyrost, potem gwałtowne narastanie05001 0001 5002 0002 5003 0003 500010203040506070Time from batch start [min]Viscosity [process units]901503501 1001 6002 3003 000Slow-increase phaseRapid-rise zone+45% in 4 min3.7 units/minFirst 10 minutes167 units/min50th–60th minute0.0 min from startviscosity 540.6 min from startviscosity 731.2 min from startviscosity 621.8 min from startviscosity 622.4 min from startviscosity 532.9 min from startviscosity 683.5 min from startviscosity 714.1 min from startviscosity 714.7 min from startviscosity 635.3 min from startviscosity 695.9 min from startviscosity 796.5 min from startviscosity 767.0 min from startviscosity 787.6 min from startviscosity 868.2 min from startviscosity 748.8 min from startviscosity 849.4 min from startviscosity 8810.0 min from startviscosity 9010.6 min from startviscosity 9511.2 min from startviscosity 10011.7 min from startviscosity 10112.3 min from startviscosity 9912.9 min from startviscosity 11013.5 min from startviscosity 10814.1 min from startviscosity 10814.7 min from startviscosity 11215.3 min from startviscosity 11915.9 min from startviscosity 12516.4 min from startviscosity 12117.0 min from startviscosity 13417.6 min from startviscosity 13718.2 min from startviscosity 13718.8 min from startviscosity 13619.4 min from startviscosity 14820.0 min from startviscosity 15320.6 min from startviscosity 15721.1 min from startviscosity 15921.7 min from startviscosity 15422.3 min from startviscosity 17222.9 min from startviscosity 17123.5 min from startviscosity 17824.1 min from startviscosity 18524.7 min from startviscosity 18125.3 min from startviscosity 17625.8 min from startviscosity 19426.4 min from startviscosity 18827.0 min from startviscosity 19927.6 min from startviscosity 20628.2 min from startviscosity 22328.8 min from startviscosity 22329.4 min from startviscosity 22930.0 min from startviscosity 22630.5 min from startviscosity 23531.1 min from startviscosity 24831.7 min from startviscosity 26332.3 min from startviscosity 28132.9 min from startviscosity 26833.5 min from startviscosity 27934.1 min from startviscosity 30334.7 min from startviscosity 30935.2 min from startviscosity 32335.8 min from startviscosity 34136.4 min from startviscosity 33137.0 min from startviscosity 36037.6 min from startviscosity 37438.2 min from startviscosity 36838.8 min from startviscosity 39939.4 min from startviscosity 39239.9 min from startviscosity 42240.5 min from startviscosity 42341.1 min from startviscosity 46241.7 min from startviscosity 49242.3 min from startviscosity 51042.9 min from startviscosity 53743.5 min from startviscosity 57744.1 min from startviscosity 57744.6 min from startviscosity 63445.2 min from startviscosity 69545.8 min from startviscosity 68046.4 min from startviscosity 67947.0 min from startviscosity 72047.6 min from startviscosity 77748.2 min from startviscosity 76648.8 min from startviscosity 87749.3 min from startviscosity 98149.9 min from startviscosity 94950.5 min from startviscosity 1,04951.1 min from startviscosity 1,01651.7 min from startviscosity 1,19952.3 min from startviscosity 1,19552.9 min from startviscosity 1,28853.5 min from startviscosity 1,47054.0 min from startviscosity 1 52454.6 min from startviscosity 1 75955.2 min from startviscosity 1 80655.8 min from startviscosity 1 76956.4 min from startviscosity 1 94557.0 min from startviscosity 2 05957.6 min from startviscosity 2 12858.1 min from startviscosity 2 38258.7 min from startviscosity 2 36059.3 min from startviscosity 2 53159.9 min from startviscosity 2 63160.5 min from startviscosity 2 65261.1 min from startviscosity 2 72461.7 min from startviscosity 2 97962.3 min from startviscosity 2 98662.8 min from startviscosity 2 91063.4 min from startviscosity 3 05164.0 min from startviscosity 2 87164.6 min from startviscosity 3 05265.2 min from startviscosity 3 01665.8 min from startviscosity 2 99066.4 min from startviscosity 3 03167.0 min from startviscosity 2 96667.5 min from startviscosity 3 01368.1 min from startviscosity 3 07068.7 min from startviscosity 3 13769.3 min from startviscosity 3 224
  • Inline measurement, 119 readings
  • Reference determinations by the plant laboratory, 7 samples
  • Rapid-rise zone, from approximately the 43rd minute

One industrial batch of UF/MUF resin, July 2026, approx. 70 minutes. Inline reading every approx. 35 s (119 points), alongside 7 reference determinations performed by the plant laboratory on the same batch. Viscosity values in process units of the installation. Hover the cursor over the chart to read a single point.

Client context

In the production of amino resins (UF, MUF), viscosity increases as polycondensation progresses, and the moment of reaction termination determines batch quality and safety. Offline measurement reflects the state from several to over a dozen minutes earlier, which, given fast kinetics, can be too late.

Delayed reaction termination risks uncontrolled viscosity growth, batch loss, and reactor blockage. The manufacturer required a product reference and reaction endpoint time indication for process control.

Challenge.

  • The reaction endpoint was assessed via manual offline rotational viscosity measurement, with information delay (dead time).
  • Risk of gelation and reactor blockage if cooling is initiated too late.
  • Manual sampling from a hot reactor exposes workers to formaldehyde vapors.
  • Lack of parameter repeatability between batches.

Solution

The Spectrally™ X1 with an immersion probe tracks polycondensation progress directly in the reactor. In the feasibility study, we developed a preliminary measurement procedure for a product reference and reaction endpoint indication.

For operation in the dense reactor medium, the probe utilizes a self-cleaning, retractable module (Retractex): it periodically retracts from the medium, flushes the optical window, and returns to measurement, maintaining a stable signal without manual cleaning during the batch.

Results

Metric Result
Polycondensation reaction endpoint Preliminary inline procedure developed (feasibility study, partial result)
Benefit Avoidance of gelation and reactor blockage, batch repeatability
Current method (offline) Manual sampling + rotational viscosity, dead time on the order of over a dozen minutes

Feasibility study result; client anonymized.

What this means for your process

If you conduct batch polycondensation of UF/MUF resins, inline reaction endpoint indication allows you to hit the process window, avoid gelation, and stabilize quality between batches, instead of controlling based on delayed laboratory viscosity.

The most reliable path to verification on a specific process is a pilot trial preceded by a short feasibility study.

Discover Gekko Photonics Solutions

Would you like to learn more about Spectrally™ analyzers? Contact our expert, who, based on a brief conversation, will advise the best measurement options for your process.

Contact Us

Find out how much you can save on your process with Spectrally™.

Contact

Aleksandra Łukasiewicz

If you are facing a similar challenge in chemical process control, quality stabilization, or real-time reaction monitoring, let's discuss a solution tailored to your technological conditions.