Olin Corporation

Maurice C Raes

John W Reisch

James M O'Connor

Curtis P Smith

Kiran B Chandalia

Michael M Martinez

Michael L Rosin

Wilhelm J Schnabel

Oliver J Proulx

Pierrepont Adams

A process for producing an ethylene oxide-capped polyol which is essentially free of catalyst residues, wherein the polyol is produced using a double metal cyanide catalyst, which comprises after polyol formation the steps of: (a) contacting a catalyst residue(s)-containing polyol with an effective amount of an oxidant (preferably selected from the group consisting of: oxygen-containing gas(es), peroxide(s), acids, and combinations thereof) to cause said catalyst residue(s) to form insoluble residues that are insoluble in the polyol; (b) separating the insoluble residues from the polyol to provide an essentially double metal cyanide catalyst residue-free polyol; (c) treating said double metal cyanide catalyst residue-free polyol with a base to provided a base-treated polyol; (d) contacting said base-treated polyol with ethylene oxide to produce an ethylene oxide-capped polyol containing base, wherein at least a portion of the secondary hydroxyl groups on said polyol are converted into primary hydroxyl groups, and (e) contacting said ethylene oxide-capped polyol containing base with an ion exchange resin in order to separate said base from said ethylene oxide capped polyol to provide a purified ethylene oxide capped polyol. In another aspect of the invention, the catalyst residue separation step is effected after EO-capping of the polyol.

Process for purifying and end-capping polyols made using double metal

This invention relates to a method of fabricating a thermoplastic elastomer which comprises the steps of: (a) fabricating a polyol having a molecular weight of between about 2,000 and about 8,000 and having a level of end group unsaturation of no greater than 0.02 milliequivalents per gram of polyol, said polyol being fabricated in the presence of a double metal cyanide catalyst, (b) reacting said polyol with a diisocyanate to produce an isocyanate-terminated prepolymer, and (c) reacting said isocyanate-terminated prepolymer with a difunctional isocyanato-reactive chain extender in a mold or in an extruder in order to produce an elastomer characterized by a hardness of between a Shore A hardness of about 50 and a Shore D hardness of about 65. Also claimed is the elastomer produced by the above method utilizing a one-shot technique.

Thermoplastic polyurethane elastomers and polyurea elastomers made using

A process for producing an ethylene oxide-capped polyol which is essentially free of catalyst residues, wherein the polyol is produced using a double metal cyanide catalyst, which comprises after polyol formation the steps of: (a) contacting a catalyst residue(s)- containing polyol with an effective amount of an oxidant (preferably selected from the group consisting of: oxygen-containing gas(es), peroxide(s), acids, and combinations thereof) to cause said catalyst residue(s) to form insoluble residues that are insoluble in the polyol; (b) separating the insoluble residues from the polyol to provide an essentially double metal cyanide catalyst residue-free polyol; (c) treating said double metal cyanide catalyst residue-free polyol with a base to provided a base-treated polyol; (d) contacting said base-treated polyol with ethylene oxide to produce an ethylene oxide-capped polyol containing base, wherein at least a portion of the secondary hydroxyl groups on said polyol are converted into primary hydroxyl groups, and (e) separating said base from said ethylene oxide capped polyol to provide a purified ethylene oxide capped polyol. In another aspect of the invention, the catalyst residue separation step is effected after EO-capping of the polyol.

The present invention relates to a process for preparing polyurethane/polyurea or polyurea elastomers by spray processing or reaction injection molding a reaction mixture comprising an A-side and a B-side, wherein said A-side comprises a polyisocyanate or an isocyanato-terminated polyurethane prepolymer and wherein said B-side comprises a polyol or polyamine plus a chain extender, in order to form a polyurethane/polyurea or polyurea elastomer, said polyol having an equivalent of between about 1,000 and about 20,000, a preferred molecular weight of between about 5,000 and about 30,000 and an end group unsaturation level of no greater than 0.06 milliequivalents per gram of polyol, said polyol being prepared using a double metal cyanide complex catalyst, said polyamine being fabricated by amine-capping said polyol with an amine-containing compound, said chain extender being selected from the group consisting of diol and aromatic diamine chain extenders with the proviso that said B-side contain at least some amount of said polyamine or of said aromatic diamine chain extender.

Preparation of elastomers using high molecular weight polyols or

This invention relates to a method of fabricating a thermoplastic elastomer which comprises the steps of: (a) fabricating a polyol having a molecular weight of between about 2,000 and about 20,000 and having a level of end group unsaturation of no greater than 0.04 milliequivalents per gram of polyol, said polyol being fabricated in the presence of a double metal cyanide catalyst, (b) reacting said polyol with a diisocyanate to produce an isocyanate-terminated prepolymer, and (c) reacting said isocyanate-terminated prepolymer with a difunctional isocyanato-reactive chain extender in a mold or in an extruder in order to produce a soft elastomer characterized by a Shore A hardness of between about 10 and about 70. Also claimed is the elastomer produced by the above method utilizing a one-shot technique.

A stable dispersion is prepared by first forming a dispersion of a polymer derived from TDI residue in an organic solvent, adding a high molecular weight polyol and then removing the solvent to produce a dispersion of the polymer in the high molecular weight polyol. In forming the dispersion in the solvent, TDI residue is reacted with an active hydrogen containing compound selected from the group consisting of an amine compound, a short-chain polyol and mixtures thereof. The stable dispersion is used in preparing a wide variety of polyurethane products, such as foams and elastomers.

Preparation of a stable dispersion from TDI residue and its use in the

A stable dispersion of a polymer in a polyol is prepared by reacting an organic polyisocyanate with a short-chain polyol in a high molecular weight polyol containing a relatively high primary hydroxyl group content, the ratio of the content of primary hydroxyl groups in the short-chain polyol to that in the high molecular weight polyol being at least a critical lower limit of about 3.5. The reaction is further carried out in the presence of a small proportion of water to achieve a reduction in the viscosity of the resulting dispersion. The dispersion is used in preparing high resilience polyurethane foam having desirable physical properties and which is of utility in a wide variety of cushioning applications.

Process for preparing a stable dispersion of a polymer in a polyol and

A selective process wherein toluene diisocyanate distillation residue is converted from a viscous liquid into an inert, granular solid by treatment with an organic acid.

Process for deactivating toluene diisocyanate distillation residue

Selected chlorine-containing methylene-bridged diaryl diisocyanates are used in the production of polyurethane foam.

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Branford, CT, United States of America

Maurice C Raes