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CAEE vs. HQEE: A Next-Generation Aromatic Diol Chain Extender for MDI Elastomers

How catechol bis(2-hydroxyethyl) ether (CAEE) improves toughness and processing over the HQEE benchmark in MDI-based polyurethane elastomers — with a high-purity, low-color grade.

Polyurethane elastomers are high-performance materials that bridge the gap between rubber and plastics, offering superior elasticity, wear resistance, and load-bearing capacity. They are synthesized by reacting three primary chemical components: diisocyanates, polyols, and chain extenders. The chain extenders are short-chain diols that react with diisocyanates to build polymer chains. Chain extenders dictate the elastomer’s performance by forming hard segments with the isocyanate that reinforce the soft polyol matrix, controlling the modulus (rigidity), tensile strength, mechanical properties, heat resistance, and abrasion resistance of the polyurethane. In Thermoplastic Polyurethanes (TPUs), diol extenders allow the hard segments to melt at high temperatures and reform when cooled, which makes the elastomer moldable and reprocessed.

Hydroquinone bis(2-hydroxyethyl) ether (HQEE) is the benchmark chain extender for high-performance polyurethane elastomers, but its high melting point and processing limitations present real challenges. Catechol bis(2-hydroxyethyl) ether (CAEE) is a new aromatic diol chain extender developed as a superior alternative for MDI-based elastomers. Across PTMEG/MDI systems (PTMEUs), CAEE delivers significantly higher tensile strength and toughness, very low tensile set, and easier one-pot processing.

Introduction

CAEE and HQEE are both aromatic diol chain extenders, but they differ in structure and behavior. CAEE has a lower melting point (84–85 °C) than HQEE (98–102 °C), which simplifies handling and processing, and it is miscible with many polyols. The structural difference — detailed below — is the basis for CAEE’s mechanical and physical performance.

The Kekulé structural formula for CAEE vs. that of HQEE is shown below.

CAEE structure
CAEE — catechol bis(2-hydroxyethyl) ether. mp 84–85 °C
HQEE structure
HQEE — hydroquinone bis(2-hydroxyethyl) ether (benchmark). mp 98–102 °C

Models show that the CAEE structure when incorporated into polyurethanes exhibits a pendant aromatic group along the polyurethane elastomer backbone. This planar aromatic structure promotes π–π interactions, leading to the formation of stacked aromatic domains within the polyurethane hard segments.

pi-pi stacking model
Conceptual π–π stacking model with CAEE.

The distillation of aromatic diols such as HQEE is difficult and uncommon due to their high boiling and melting points, and the tendency to generate color and degradation products at distillation temperatures. However, CAEE can be vacuum distilled under controlled conditions to yield a chain extender with a distinctly white appearance relative to crystallized CAEE.

pellet comparison
CAEE product comparison: crystallized (off-white to yellow) vs. distilled (white) pellets.

Performance Enhancements with CAEE

Use of distilled CAEE as a chain extender produces polyurethane elastomers that are visibly whiter than elastomers prepared with recrystallized CAEE. Cast, molded, or extruded articles prepared using distilled CAEE exhibit high initial whiteness and maintain color more consistently during storage and service. Polyurethanes manufactured with distilled CAEE also exhibit enhanced mechanical properties and greater consistency compared to polyurethanes produced using only recrystallized CAEE, as shown below.

Property (PTMEG 2000 / MDI) Crystallized CAEE Distilled CAEE
Hardness, Durometer A 87 / 86 88 / 86
Rebound Elasticity 52% 56%
Ultimate Tensile Strength 7,169 psi 7,368 psi
Ultimate Elongation 540% 530%
Strength (work energy to break) 855 in-lbs 866 in-lbs
Tensile Modulus (500%) 5,100 psi 5,250 psi
Tensile Set – 30 min 6% 6%
Die C Tear (D624) 504 pli 582 pli
Clarity Clear Opaque
Gel Time (min) 7 7

The practical payoff of the CAEE hard-segment structure is a step-change in mechanical performance: across PTMEG/MDI systems CAEE outperforms the HQEE benchmark on tensile strength, toughness, and tensile set — while processing more simply.

CAEE vs. HQEE in PTMEG/MDI (PTMEU)

In processing, CAEE is compatible with a simplified one-pot process, whereas HQEE requires pre-blending with PTMEG to suppress freezing. To keep reaction conditions consistent across both systems, both CAEE and HQEE were run as blends in the PTMEG polyols, allowing a representative comparison. MDI was introduced at 20 °C and the mix held at 85 °C (FlackTek™, 1200 rpm, 1.5 min, vacuum degassing), then cast and post-cured (gel times >4 min; cure 100 °C for 10 hours).

Formulation Durometer A/D Tensile (psi) Tensile Set % Elong. % Die C Tear (pli) 1938 Tear (pli) Ball Rebound RT %
MDI / PTMEG 1000 / HQEE 60D 4,790 14 180 628 107
MDI / PTMEG 1000 / HQEE 93A 5,013 8 280 644 106 30
MDI / PTMEG 1000 / HQEE 85A 5,268 7 350 462 80 19
MDI / PTMEG 2000 / CAEE 56D 8,078 21 500 967 382 53
MDI / PTMEG 1000 / CAEE 93A 8,117 3 480 559 183 26
MDI / PTMEG 1000 / CAEE 82A 5,832 −2 450 420 84 20

The combination of high tensile strength, high elongation, and very low tensile set indicates minimal phase mixing in the CAEE–MDI hard block. CAEE PTMEU systems show tensile set of −2% and +3%, versus 7–8% for the corresponding HQEE systems — evidence of an effective hard-block structure with minimal molecular slippage.

Results: Strength and Toughness

Across PTMEG/MDI systems, CAEE tensile strengths are significantly higher than comparable HQEE and 1,4-BDO systems at every Durometer hardness, and elongation is higher as well — so CAEE-based polyurethanes are consistently tougher.

The tensile strength of PTMEG/MDI systems chain extended with CAEE, HQEE or 1,4-BDO are compared in the chart below. CAEE tensile strengths and elongation values are significantly higher than the comparable HQEE and BDO systems, at all Durometer values. The result is that the PTMEG/MDI/CAEE based polyurethanes are consistently much tougher.

tensile-strength-chart-1

Tensile Strength of PTMEG/MDI/Chain Extender vs. Durometer (CAEE / HQEE / BDO). Source: PMA 2026 poster chart.
The stress-strain graphs below compare one-shot PTMEG 1000/MDI elastomers chain extended with CAEE and HQEE. At an equivalent hardness of 93A, the CAEE elastomer energy absorption before rupture is 741 in-lbs., about 2.9 times greater than that of the HQEE elastomer. The CAEE based PTMEUs are significantly tougher than other PTMEUs.
stress strain 93A
CAEE vs. HQEE in the 93A PTMEU elastomer — stress–strain curve and energy absorption.

CAEE with various polyols

CAEE also performs across polyol families — PTMEG, polycaprolactone (PCL), PO3G (poly(trimethylene ether) glycol), adipate polyester polyols, and a HDO-based polycarbonate polyols. The results with PCL are particularly striking: CAEE and PCL 2000 polyols are miscible at 60 °C, and at 94A Durometer the elastomer reached a tensile stress above 8,000 psi without deformation or break, with a notable 826 in-lbs. of energy absorption. The 94A elastomer also held a stable Durometer value over time, showing no cold hardening affects.

Formulation Durometer A/D Tensile (psi) Tensile Set % Elong. % Die C Tear (pli) 1938 Tear (pli) Ball Rebound RT %
MDI / PTMEG 2000, CAEE, Dabco/T-12 89 7,169 6 540 504 194 52
MDI / PCL 2000, CAEE, Dabco/T-12 94 >8,000 8 550 813 420 34
MDI / PO3G, CAEE, T-12 93 5,268 8 545 620 225 27
MDI / Polyester 2000 / CAEE 92 6,051 6 600 656 416 29
MDI / PCD 2000 / CAEE 88 6,350 2 565 446 226 25

Processing Example: MDI / PTMEG / CAEE

CAEE is an excellent, compatible chain extender for MDI/PTMEG systems. The following examples show the high physical properties achievable with the PTMEG/MDI/CAEE system.

Two formulations are shown below in the 90–95A Durometer hardness range — Formulation 1 with PTMEG 1000 and Formulation 2 with PTMEG 2000. The MDI is a carbodiimide-modified MDI (Cosmonate LL, 29.4% NCO). The catalyst in Formulation 2 was a blend of 1 drop of DABCO 33LV and 1 drop of a 20:1 blend of a 3000 MW PPG diol and T-12.

Component (grams) Formulation 1 (PTMEG 1000) Formulation 2 (PTMEG 2000)
CM-MDI (Cosmonate LL) 90.16 67.79
PTMEG 121.83 (OH 113.4) 149.6 (OH 56.7)
CAEE (OH 545.20) 38.01
CAEE (OH 543.03) 32.37
Catalyst None 1 drop each
Mix temperature CAEE/PTMEG at 90 °C, CLL at 20 °C All at 70 °C

PTMEG, CAEE, and catalyst (where used) were mixed, thoroughly degassed, and conditioned to the temperatures shown to form a homogeneous solution. The MDI, at room temperature, was then added and final mixing done in a FlackTek machine under vacuum at 1000 rpm — 1.5 min for Formulation 1 and 2 min for Formulation 2. Molds were preheated to 110 °C, and the mixtures poured easily into the aluminum molds. Gel times were approximately 10 minutes for Formulation 1 and 7 minutes for the catalyzed Formulation 2. Total cure time was 10 hours at 110 °C, with demolding after about 1 hour.

Property Formulation 1 Formulation 2
Durometer A 94 91
Tensile (psi) 8,117 7,368
Elongation (%) 480 530
Tensile Set (%) 3 6
Energy Absorption (in-lb) 741 866
Die C Tear (pli) 559 582
1938 Tear (pli) 183 180
Rebound (%) 26 56

At equal hardness, the CAEE elastomers show up to approximately three times the toughness — energy absorption before rupture — of the corresponding HQEE elastomers.

Performance–Temperature Profiles

Dynamic mechanical analysis (ASTM D4065) on laboratory plaques shows very good phase separation for CAEE, reflected in its low glass-transition temperature. The lower tan δ for CAEE indicates lower rolling resistance and energy absorption.

DMA — MDI-PTMEG 2000; 85 Shore A CAEE-(PTMEU) HQEE-(PTMEU)
Tg −55 °C −34 °C
Tm 142 °C 157 °C
Tan δ (Delta) @ 20 °C 0.094 0.12

At 82–83A Durometer (PTMEG 1000/MDI), the temperature profiles of CAEE and HQEE elastomers are quite similar, and both show excellent resiliency and rebound.

durometer-vs-temp-chartdurometer-vs-temp-chart
Durometer vs. Temperature (°C).
rebound-vs-temp-chartrebound-vs-temp-chart
Rebound % vs. Temperature (°C).

A MOCA-Free Aromatic Chain Extender

CAEE offers a MOCA-free route to high-performance polyurethanes. For formulators facing tightening restrictions and customer pressure to replace MOCA, CAEE/MDI systems offer the mechanical properties, toughness, and processing advantages described above.

Applications

CAEE’s combination of toughness, processing ease, and color stability suits demanding, high-performance polyurethane applications, including:

  • High-load industrial wheels & tires, forklift tires
  • Recreational wheels
  • Pipe linings & protective coatings
  • Paper machine filtration fabrics, shoe press sleeves
  • Seals, gaskets & sprockets
  • Belting & conveyor systems
  • Oil field & mining components
  • Other high-performance polyurethane applications

Conclusion

CAEE represents a next-generation aromatic diol chain extender:

  • Very high tensile, elongation, energy absorption, and toughness
  • Low tensile set values — efficient hard-segment formation
  • Excellent low-temperature flexibility and high-temperature properties
  • Suitable for one-pot, pre-polymer, and quasi-systems
  • Excellent flow in a TPU with no loss of physicals when processed at 400 °F
  • Distilled CAEE is white with a low discoloration tendency

CAEE outperforms the HQEE benchmark across every polyol system tested — higher tensile strength, greater toughness, lower tensile set — while processing more simply. Distilled CAEE is a whiter, more consistent product.

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