High Performance Polymerization Inhibitors

What is high performance polymerization inhibitor?

Mechanism of Polymerization Inhibition (Presumed)

In the cases of Q-1300 and Q-1301

Polymerization inhibition mechanism of high-performance polymerization inhibitor (assumed)

The nitroso group catches a radical in the system, and (1) is formed.
Attack of (1) to monomer causes a reaction with propagating radical to form a stable coupling product (2).
N-N cleavage of coupling product (2) proceeds at the temperature of 50°C or higher and forms a product (3).
Furthermore, the product (3) reacts with 2 radicals to form a product (4).

In the case of benzoquinone1)

Benzoquinone polymerization inhibition mechanism
1) J.C. Bevington, N.A. Ghanen, H.W. Melville, Trans. Faraday Soc. 51 346(1995) ; J. Chem.Soc. 1955 2822

In the case of nitroso compounds2)

Polymerization inhibition mechanism of nitrosobenzene
2) Polymer Bulletin 33,325-329(1980)

Comparison of Polymerization Inhibiting Effects

Measurement conditions
  • Purified styrene
  • Concentration of polymerization inhibitor: 1,000 ppm
  • Heating temperature: 120°C
  • Under nitrogen gas flow
Graph showing higher residual monomer ratio when using Q-1300 or Q-1301 than when using other polymerization inhibitors

⇒ Q-1300 and Q-1301 show stronger polymerization inhibiting effect than other polymerization inhibitors at high temperature.

Examples of Applications

  • Preservative stabilizer (monomers, UV inks, UV paints, and photosensitive resins).
  • Prevention of polymerization during distillation of monomers.
  • Prevention of polymerization during production of monomers and oligomers, and during heating/mixing of monomers.
  • Suspension of polymerization when an abnormal polymerization is observed.
  • Suspension of polymerization once the target polymerization rate is attained.

Thermal Polymerization Inhibiting Effect

Q-1300 and Q-1301 show an excellent inhibiting effect in thermal polymerization.

Acrylic acid3)

The formation level of polymerized product was comparatively-measured based on the change of relative viscosity of the solution which was heated for a certain period of time under the existence of polymerization inhibitor.

Measurement conditions
  • 50% Acrylic acid water solution, polymerization inhibitor concentration of 1,000 ppm/monomer
  • Heating temperature: 100°C
  • Heating time: 8 hours
  • Under nitrogen gas flow

Relative viscosity of acrylic acid water solution before and after heating

Polymerization inhibitor Relative viscosity (30°C)
No addition, before heating 1.77
Hydroquinone monomethyl ether Unmeasurable because of high viscosity
Q-1300 1.77
3) Japan Examined Patent Application Publication No. Sho-39-220 Nitto Rikagaku Kogyo Co., Ltd.

Polyfunctional vinyl monomer4)

The thermal stability of polyfunctional vinyl monomer composition was measured.

Composition of monomer

2-Propenoic acid, 2-methyl-, 1,1′-[(1-methylethylidene)bis[(2,6-dibromo-4,1-phenylene)oxy-2,1-ethanediyl]] ester CAS RN:67006 -39-7 60 part
Divinylbenzene 20 part
Chlorostyrene(o-/p-=65/35) 20 part
Measurement conditions
  • Heating temperature: 70°C

Comparison of thermal stability

Polymerization inhibitor Addition amount (ppm) Result
Blank - Increase of viscosity after 5 hours
Hydroquinone monomethyl ether 500 Increase of viscosity and gelation after 3 hours
Q-1301 5 No increase of viscosity and gelation, even after 15 hours
4) JP-A-Sho-63-170401 Toray Industries, Inc.

Polymerization Inhibiting Effect in Distillation (Heating and Reduced Pressure)

Q-1300 and Q-1301 show an excellent inhibiting effect in distillation (heating and reduced pressure).

Acrylic acid5)

The inhibiting effect of the product when used for purification of acrylic acid by distillation was measured.

Measurement conditions
  • Acrylic acid: 1 L
  • Distillation temperature: 103°C/20 kPa

Comparison of polymerization inhibiting effect

Polymerization inhibitor Addition amount (ppm) Result
Manganese acetate Hydroquinone monomethyl ether 500
200
Formation of polymerized product was observed in the container and the distillation column after approximately 300 ml of distillate was obtained.
Manganese acetate Q-1300 20
20
Formation of polymerized product was not observed.
5) EP 301879(1989) Hoechst Celanese

Dimethylaminoethyl methacrylate6)

The effect of polymerization inhibitor was measured when synthesizing dimethylaminoethyl methacrylate by transesterification reaction, followed by separation and purification by distillation.

Measurement conditions

【Transesterification reaction】

  • Methyl methacrylate: 750 g (7.5 mol)
  • Dimethylaminoethanol: 268 g (3.0 mol)
  • Pb: 12.4 g (0.06 mol)
  • Reaction temperature: 65-70°C
  • Reaction time: 4.5 hours

【Purification by distillation】

  • Distillation temperature: 72°C/2.4 kPa - 63.5°C/0.7 kPa

Comparison of the inhibiting effects in transesterification reaction

Polymerization inhibitor Addition amount (g) Yield (%) Residue (g) Remark
Hydroquinone monomethyl ether 3.0 - - Polymerizing during reactions
Q-1300 2.3 91.5 13.2
6) JP-A-Sho-52-153912 Nitto Chemical Industries Co., Ltd.

Radical Polymerization Inhibiting Effect

Vinyl chloride

During polymerization of vinyl chloride, stirring and cooling were stopped, and the change in temperature over time was measured after the addition of polymerization inhibitor.

Measurement conditions
  • Vinyl chloride: Water = 1: 1.2, PVA 0.08%
  • Radical polymerization initiator: V-65 (0.03%)
  • Polymerization temperature: 56.5°C
  • Q-1300: 100 ppm
  • After five hours of polymerization, stirring and cooling in the system were stopped, and the polymerization inhibitor was added one minute later.
Graph showing the polymerization inhibition effect of Q-1300

⇒  Q-1300 has an excellent inhibiting effect in suspension polymerization.

Measurement of the Induction Period of Radical Polymerization

Sodium acrylate

The inhibiting effect of polymerization inhibitor in the water solution polymerization of sodium acrylate was evaluated.

Measurement conditions
  • Monomer concentration: 20% (w/v)
  • Polymerization inhibitor: 2,000 ppm/monomer
  • Radical polymerization initiator for water solution:V-50 (0.4%/monomer)
  • Polymerization temperature: 50°C
Graph showing the induction period and inhibition effect of Q-1300 in the aqueous polymerization of sodium acrylate.

Acrylamide

The inhibiting effect of polymerization inhibitor in the water solution polymerization of acrylamide was evaluated.

Measurement conditions
  • Monomer concentration: 50% (w/v)
  • Polymerization inhibitor: 2,000 ppm/monomer
  • Radical polymerization initiator for water solution:V-50 (1.0%/monomer)
  • Polymerization temperature: 50°C
Graph showing the induction period and inhibition effect of Q-1300 in the aqueous solution polymerization of acrylamide.

⇒  Q-1300 has a longer induction period and a stronger inhibiting effect as compared with other polymerization inhibitors.

Propagation Inhibiting Effect in the Case of Abnormal Polymerization

The product inhibits propagation of popcorn polymer* and shows a higher inhibiting effect than other inhibitors.

* Popcorn polymer: Generic name of less soluble and less meltable polymers formed by three-dimensional crosslinking of monomers during distillation.

Glycidyl methacrylate7)

We compared the growth of popcorn polymers under the condition of existence of polymerization inhibitor in the glycidyl methacrylate polymerization system.

Measurement conditions
  • Glycidyl methacrylate: 30 part Methyl acrylate: 20 part Water:1,500 part
  • Polymerization inhibitor: 1,000 ppm/monomer Polymerization temperature: 35°C Polymerization time:10 hours
  • Polymerization initiator: APS-Na2SO3 Water-based redox polymerization

Inhibiting effect in the case of abnormal polymerization

Inhibitor Polymerization yield Specific viscosity of polymer Remark
Blank 87.3 0.124 Popcorn monomer 2.7 part formed
Q-1300 92.7 0.122 No popcorn polymer formed
7) Japan Examined Patent Application Publication No. Sho-48-2934

Acrylic acid8)

Nucleus of popcorn polymer (SBR) was placed in the gas phase under the reflux condition of acrylic acid, and the change of mass of the popcorn polymer was measured.

Measurement conditions
  • Reflux under reduced pressure (6.7 kPa), reaction time: 6 hours

Inhibiting effect in the case of abnormal polymerization

Inhibitor Addition amount (ppm) Change of mass of popcorn nucleus (%)
Phenothiazine 126 +636
Q-1300 102 0.0
8) USP 4772740(1988) Mallinckrodt

Methyl methacrylate8)

Nucleus of popcorn polymer (SBR) was placed in the gas phase under the reflux condition of methyl methacrylate and the change of mass of the popcorn polymer was measured.

Measurement conditions
  • Reflux under reduced pressure (6.7 kPa), reaction time: 6 hours
  • The inhibitor was divided into six parts and added each part every an hour.

Inhibiting effect in the case of abnormal polymerization

Inhibitor Addition amount (ppm) Change of mass of popcorn nucleus (%)
Phenothiazine The same mole quantity as that of Q-1300 +237
Hydroquinone The same mole quantity as that of Q-1300 +243
Q-1300 100 +18
8) USP 4772740(1988) Mallinckrodt