JUN 9, 202662 MINS READ
Triethylene glycol material possesses a linear molecular architecture comprising three ethylene oxide units terminated by hydroxyl groups (-OH), conferring amphiphilic character essential for its multifunctional applications. The compound exhibits a boiling point of approximately 287.4°C at atmospheric pressure and a melting point ranging from -7°C to -4°C, enabling liquid-phase operation across broad temperature windows 7,10. Its density at 20°C is approximately 1.125 g/cm³, with dynamic viscosity of 47.8 mPa·s at 20°C, significantly higher than monoethylene glycol (16.1 mPa·s) but lower than tetraethylene glycol, reflecting the balance between molecular weight and intermolecular hydrogen bonding 10.
The hygroscopic nature of triethylene glycol material stems from extensive hydrogen bonding networks formed by terminal and ether oxygen atoms, yielding water miscibility in all proportions and solubility in polar organic solvents including alcohols, ketones, and esters 1,7. This property underpins its efficacy in gas dehydration applications where moisture removal efficiency exceeds 99% under optimized conditions 7,10. Refractive index (nD²⁰) of 1.4559 and dielectric constant of approximately 23.7 at 25°C further characterize its optical and electrical properties, relevant for formulation in electronic materials and dielectric fluids 10.
Thermal stability analysis via thermogravimetric analysis (TGA) demonstrates onset decomposition temperature above 200°C under inert atmosphere, with 5% weight loss occurring at approximately 220°C, though prolonged exposure above 180°C may induce oxidative degradation and color formation in the presence of oxygen 10. The flash point (closed cup) of 177°C and autoignition temperature of 371°C classify TEG as a combustible liquid requiring standard fire safety protocols during storage and handling 10.
The predominant industrial synthesis of triethylene glycol material involves controlled addition polymerization of ethylene oxide (EO) to ethylene glycol or diethylene glycol under alkaline catalysis 6,7. In a representative process, triethylene glycol of ≥99.95% purity serves as the starting material, combined with 0.005-1.0 wt% (preferably 0.01-0.5 wt%) of alkali catalyst such as sodium hydroxide or potassium hydroxide 6. Prior to EO addition, the feedstock undergoes rigorous dehydration at 70-150°C under reduced pressure (0-0.013 MPa) with nitrogen sparging for 0.5-3 hours to eliminate residual water and minimize formation of lower glycol homologs (ethylene glycol and diethylene glycol) 6.
The polymerization reaction proceeds at 80-230°C (optimally 120-180°C) under controlled pressure of 0-1 MPa (preferably 0.2-0.6 MPa), with ethylene oxide introduced incrementally to maintain exotherm control and molecular weight distribution 6. This methodology yields polyethylene glycol products with average molecular weights ranging from 190 to 1,050 g/mol, wherein triethylene glycol represents the trimer fraction 6. Ethylene glycol and diethylene glycol by-product contents are maintained below 0.5 wt% and 1.0 wt% respectively through optimized reaction kinetics and subsequent distillation purification 6,7.
Recovery of high-purity triethylene glycol material from mixed glycol compositions generated in ethylene oxide hydration processes employs multi-stage fractional distillation with pH control 7. The feed stream, typically containing monoethylene glycol (MEG), diethylene glycol (DEG), and triethylene glycol (TEG), undergoes initial distillation under reduced pressure (50-100 mmHg) to separate MEG overhead, yielding a bottoms fraction enriched in DEG and TEG 7. Critical to product quality, the pH of this bottoms stream is adjusted to 6.0-8.5 using mineral acids (phosphoric acid, sulfuric acid) or organic acids (citric acid) prior to subsequent distillation stages 7.
The pH-adjusted DEG/TEG mixture is then distilled to recover DEG overhead, with the TEG-rich bottoms again pH-adjusted to 6.0-8.5 before final distillation to obtain triethylene glycol material of >99% purity as overhead product 7. This pH control strategy significantly reduces thermal degradation and color formation (APHA color index <15) compared to conventional distillation without pH adjustment, while increasing TEG recovery yield by 5-12% 7. The process demonstrates particular efficacy in separating TEG from structurally similar triols such as glycerine and 1,2,4-butanetriol, which exhibit nearly identical boiling points but can be differentiated through azeotropic distillation using entrainers like p-xylene, α-pinene, or diisobutyl ketone 18.
Triethylene glycol material serves as a versatile precursor for functional derivatives through esterification reactions with carboxylic acids 2,9,12,14. A notable example involves synthesis of triethylene glycol disorbate, a low-VOC coalescent for coating formulations, via reaction of TEG with sorbic acid in the presence of sulfuric acid catalyst (0.001-3 wt%) and aprotic azeotropic solvent at 90-160°C 9,14. Optimized conditions yield disorbate:monosorbate weight ratios of 19:1 to 99:1, with the high disorbate purity (>95%) meeting stringent VOC regulations while maintaining non-crystalline character essential for coalescent function 2,9,14.
Similarly, triethylene glycol-based plasticizers for polyvinyl chloride (PVC) are synthesized by reacting TEG (10-40 wt%) with C₃-C₁₂ aliphatic acids (1-80 wt%) and C₆-C₁₀ aromatic acids (1-60 wt%) in the presence of 0.001-3 wt% esterification catalyst 3,12,15. The resulting mixed esters, exemplified by 2-(2-(2-(2-ethylhexanoyloxy)ethoxy)ethoxy)ethyl 2-ethylhexanoate and 2-(2-(2-phenylcarbonyloxyethoxy)ethoxy)ethyl benzoate, impart superior plasticization efficiency, low volatility (heating loss <2% at 80°C/24h), high elongation (>350%), and excellent transparency to PVC formulations compared to conventional phthalate plasticizers 3,12,15.
High molecular weight TEG-POE IV polymers represent a significant advancement in surface-eroding biodegradable materials for drug delivery and medical implant applications 8. These polymers are synthesized through polycondensation of triethylene glycol with orthoester monomers, achieving molecular weights ranging from 10,000 to 150,000 g/mol without altering the diol composition 8. The synthesis methodology enables precise control over degradation kinetics by varying the triethylene glycol to triethylene glycol-glycolide ratio while maintaining consistent molecular weight, a critical parameter for tailoring drug release profiles 8.
TEG-POE IV polymers exhibit surface erosion mechanisms characterized by hydrolytic cleavage of orthoester linkages under mildly acidic conditions (pH 5.0-6.5), with degradation rates tunable from days to months depending on polymer composition and molecular weight 8. Mechanical properties include tensile strength of 15-45 MPa and elongation at break of 200-600%, significantly superior to conventional poly(lactic-co-glycolic acid) (PLGA) systems 8. Biocompatibility studies demonstrate minimal inflammatory response and complete resorption within predetermined timeframes, making these materials suitable for dental applications, wound healing matrices, and sustained-release drug delivery systems 8. Formulations incorporating collagen or other biologically active additives further enhance tissue integration and therapeutic efficacy 8.
Poly(trimethylene-ethylene ether) glycol, synthesized via polycondensation of 1,3-propanediol with ethylene glycol or its oligomers (degree of polymerization 3-4), represents a novel class of polyether diols with molecular weights ranging from 250 to 10,000 g/mol (preferably 1,000-5,000 g/mol) 11. The alternating trimethylene and ethylene oxide segments confer unique crystallization behavior and mechanical properties distinct from homopolymer polyethylene glycol or polytrimethylene glycol 11. These copolymers exhibit melting points of 20-55°C depending on molecular weight and composition, with glass transition temperatures (Tg) ranging from -70°C to -50°C 11.
Applications span thermoplastic polyurethane (TPU) soft segments, where the copolymer structure provides enhanced hydrolytic stability and lower water absorption compared to conventional polyether glycols, yielding TPUs with improved dimensional stability in humid environments 11. Incorporation of additives including delustrants, colorants, stabilizers (hindered phenols, phosphites), flame retardants, and antimicrobial agents enables tailored performance for specific end-uses in automotive interiors, footwear, and medical tubing 11. The copolymer's balanced hydrophilicity and crystallinity also render it suitable for personal care formulations and as a reactive intermediate in specialty coatings 11.
These oligomeric diols, characterized by the structure HO-[(-OCH₂CH₂CH₂O-)z-CO-]n-H where z=1-10 and n=2-100, are synthesized via cationic ring-opening polymerization of trimethylene carbonate using acidic ion exchange resin catalysts in aprotic solvents at 30-250°C 19. The process yields hydroxyl-terminated oligomers with controlled molecular weight distribution and carbonate-to-ether linkage ratios, enabling precise tuning of thermal and mechanical properties 19. Number-average molecular weights (Mn) typically range from 500 to 15,000 g/mol, with polydispersity indices (PDI) of 1.2-2.0 19.
These materials exhibit glass transition temperatures of -60°C to -20°C and melting points of 30-80°C depending on carbonate content, with tensile moduli of 5-50 MPa and elongation at break exceeding 500% 19. The carbonate linkages impart superior hydrolytic stability and oxidative resistance compared to polyether or polyester diols, while maintaining biodegradability under enzymatic or alkaline conditions 19. Applications include soft segments for high-performance polyurethanes, biomaterials for tissue engineering scaffolds, and reactive oligomers for UV-curable coatings 19. The diol functionality enables facile chain extension with diisocyanates or incorporation into polycarbonate-polyurethane (PC-PU) block copolymers exhibiting exceptional mechanical strength and biocompatibility 19.
Triethylene glycol material dominates natural gas dehydration applications due to its optimal balance of hygroscopicity, thermal stability, and regenerability 7,10. In typical glycol dehydration units, wet natural gas contacts counter-current flowing TEG solution (95-99 wt% concentration) in absorption towers operating at 30-50°C and 40-100 bar, achieving water removal to dew points of -40°C to -60°C 10. The water-rich glycol (85-92 wt% TEG) is then regenerated in reboiler-stripper systems at 180-205°C under atmospheric or slight vacuum, restoring TEG concentration to >98.5 wt% for recycle 10.
TEG's superior performance versus monoethylene glycol and diethylene glycol stems from lower vapor pressure (0.01 mmHg at 20°C vs 0.12 mmHg for DEG), enabling higher regeneration concentrations and reduced glycol losses to gas phase 7,10. Corrosion inhibition is achieved through formulations containing 0.1-1.0 wt% soluble borate compounds and 0.01-0.5 wt% Group VIa metal oxygenates (chromate, molybdate, tungstate), which passivate carbon steel surfaces and maintain pH 7.5-9.0 10. Addition of 0.05-0.2 wt% copper corrosion inhibitors (benzotriazole, tolyltriazole) protects brass and bronze components in heat exchangers 10.
Hydrogen sulfide scavenging formulations combine triethylene glycol material (15-95 wt%, preferably 15-50 wt%) with triazine compounds formed by reacting monoethanolamine with formaldehyde, optionally including diglycolamine as a secondary amine 16. These formulations effectively remove H₂S and mercaptans from gaseous and liquid hydrocarbon streams while minimizing solid dithiazine deposits that plague conventional triazine scavengers 16. The TEG component solubilizes reaction products and maintains fluidity at low temperatures, with scavenging capacities exceeding 2.0 kg H₂S per kg formulation under field conditions 16.
Single-phase heat transfer fluids based on triethylene glycol material exhibit thermal stability from -20°C to 230°C, with formulations containing 50-95 wt% TEG, 5-50 wt% water, and corrosion inhibitor packages comprising 0.5-3.0 wt% soluble borates and 0.1-1.0 wt% molybdates or tungstates 10. These fluids demonstrate specific heat capacity of 2.3-2.8 kJ/(kg·K) at 100°C, thermal conductivity of 0.25-0.30 W/(m·K), and kinematic viscosity of 8-15 mm²/s at 40°C 10. The high boiling point and low vapor pressure enable operation in closed-loop systems at elevated temperatures without pressurization, reducing equipment costs and safety risks compared to mineral oil or synthetic hydrocarbon fluids 10.
Corrosion testing per ASTM D1384 shows weight loss <10 mg/cm² for carbon steel, copper, brass, solder, and aluminum coupons after 336 hours at 88°C, meeting automotive and industrial coolant specifications 10. The formulations exhibit pH stability (7.5-9.5) over 2,000 hours at 150°C, with reserve alkalinity >5.0 mL 0.1N HCl per 10 mL sample, ensuring long-term corrosion protection 10. Freeze protection to -15°C is achieved with 60:40 TEG:water blends, while 80:20 blends provide protection to -30°C 10. Applications span solar thermal systems, industrial process heating, and data center cooling infrastructure where non-toxic, thermally stable fluids are mandated 10.
Triethylene glycol-based ester plasticizers for PVC exhibit migration resistance, low volatility, and excellent low-temperature flexibility
| Org | Application Scenarios | Product/Project | Technical Outcomes |
|---|---|---|---|
| DOW GLOBAL TECHNOLOGIES LLC | Low-VOC coating formulations requiring effective coalescent agents for paint and surface coating applications with stringent environmental regulations. | Triethylene Glycol Disorbate Coalescent | Achieves disorbate to monosorbate weight ratio of 19:1 to 99:1, meeting low VOC requirements while maintaining non-crystalline properties essential for coalescent function in coating formulations. |
| LG CHEM LTD. | Polyvinyl chloride (PVC) resin formulations for food packaging films, flexible tubing, and consumer products requiring non-toxic plasticizers with high performance characteristics. | Triethylene Glycol Ester Plasticizer | Provides low heating loss (<2% at 80°C/24h), high elongation (>350%), excellent transparency, and superior plasticization efficiency compared to conventional phthalate plasticizers for PVC applications. |
| UNION CARBIDE CORPORATION | Single-phase heat transfer systems including solar thermal installations, industrial process heating, and data center cooling infrastructure requiring non-toxic, thermally stable fluids. | Triethylene Glycol Heat Transfer Fluid | Delivers thermal stability from -20°C to 230°C with corrosion inhibition through soluble borate and Group VIa metal oxygenate compounds, maintaining pH 7.5-9.5 and preventing corrosion in multi-metal systems. |
| EVONIK OPERATIONS GMBH | Medical implants, dental applications, wound healing matrices, and sustained-release drug delivery systems requiring biocompatible and biodegradable polymer materials. | TEG-POE IV Biodegradable Polymer | Achieves molecular weights of 10,000-150,000 g/mol with surface-eroding biodegradation, tensile strength of 15-45 MPa, and tunable degradation rates from days to months for controlled drug release. |
| NOF CORPORATION | Pharmaceutical formulations, polymer synthesis intermediates, and specialty chemical applications requiring high-purity polyethylene glycol with controlled molecular weight distribution. | High Purity Polyethylene Glycol | Produces polyethylene glycol with average molecular weight 190-1,050 g/mol containing minimal ethylene glycol (<0.5 wt%) and diethylene glycol (<1.0 wt%) through optimized ethylene oxide polymerization with triethylene glycol feedstock. |