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A method of obtaining a molded urethane elastomers

A method of obtaining a molded urethane elastomers
IPC classes for russian patent A method of obtaining a molded urethane elastomers (RU 2107073):
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(57) Abstract:

The invention relates to methods for molding urethane elastomers with high strength properties and may find application in engineering, for example, for the manufacture of coating rolls of paper machines, rollers assemblies of sheet metal and other bulky items. The method of obtaining castable urethane elastomers lies in the interaction of the prepolymer on the basis of polyoxyethyleneglycol and 2,4-toluylene diisocyanate with a content of isocyanate groups of 6.1 to 7.2% with a solution of 3,3'-dichloro - 4,4' -diaminodiphenylmethane in two - or trifunctional polyetherpolyols and the prepolymer at a molar ratio of 3,3' -dichloro - 4,4'- diaminodiphenylmethane, polyetherpolyols and prepolymer equal(0,87 - 0,90) : (0,10 - 0,13) : 0,05 when using the bifunctional polyester and(0,94 - 0,95) : (0,05 - 0,06) : 0,05 when using trifunctional polyester, respectively, per 1 mol of the initial prepolymer. Application for dissolution of 3,3' -dichloro - 4,4'-diaminodiphenylmethane except polyetherpolyols, the prepolymer with terminal isocyanate groups allows to obtain a stable at room temperature a solution with high concentration is and properties and high viability of the reaction mass, which is very important for the manufacture of roll covers and other large items. table 1.

The invention relates to the production of polymeric materials and can be used for the manufacture of coating rolls of paper machines, rollers assemblies of sheet metal, rolls for textile machines, coating calender rolls used in the manufacture of magnetic tapes and for the manufacture of other large items.

A method of obtaining castable urethane elastomers by reacting the prepolymers with terminal isocyanate groups with molten diamine - 3,3'- dichloro - 4,4'- diaminodiphenylmethane (P. Wright and other Polyurethane elastomers. Chemistry, 1973; Urethane elastomers. Ed. by N. P. Apukhtin. L.: Chemistry, 1971). The elastomers obtained by a specified method, have high strength properties (tensile strength at break of 40-50 MPa).

The disadvantage of this method is the low viability of the reaction mass (5-10 min) after injection of molten diamine, which greatly complicates the manufacture of large-sized products.

The number of known methods for obtaining molded urethane elastomers, which increases the of groups with a solution of 3,3'-dichloro-4,4'-diaminodiphenylmethane in various polyether polyols for example, a copolymer of propylene oxide and tetrahydrofuran (ed. St. USSR N 553259).

However, the elastomers obtained by a specified method, have low strength characteristics (p12,0 MPa) and are mainly used as sealants.

A method of obtaining castable urethane elastomers by reacting the prepolymer with terminal isocyanate groups, obtained on the basis of polybutadiene and 2,4-toluylene diisocyanate with a solution of 3,3'-dichloro-4,4'-diaminodiphenylmethane simple polyetherpolyols, which used a copolymer of propylene oxide and ethylene oxide with a mole.mass 5000 ( ed. St. USSR N 1597365, class C 08 G 18/32).

This method is adopted for the prototype. The elastomers obtained by the described method, are mainly used as a binder for composite materials, the disadvantages are their low strength properties, the tensile strength is less than 7.3 MPa at 23oC.

The purpose of the invention to provide a castable urethane elastomers with high strength properties while maintaining high viability of the reaction mass.

The aim is achieved in that in a method of producing injection molded urethanes is unctionally of polyether polyols and prepolymer-based polyoxyethyleneglycol and 2,4 - toluylene diisocyanate with a content of isocyanate groups of 6.1 - 7.2% in the following molar ratio of diamine : the bifunctional polyol : a prepolymer: (0,87-0,9) : (0,1-0,13) : 0,05; diamine : trifunctionally polyol : a prepolymer(0,94-0,95) : (0,05-0,06) : 0,05 on 1 mol of the initial prepolymer.

First preparing a saturated solution of 3,3'-dichloro-4,4'-diaminodiphenylmethane in polyetherpolyols at a temperature of 85-105oC, and then at a temperature of 95-100oC add a prepolymer with terminal isocyanate groups, which chemically binds the excess of diamine in excess of the limit of its solubility at a temperature of 25-30oC, and the resulting liquid diamine also dissolves part of 3,3'-dichloro-4,4'-diaminodiphenylmethane.

So, get stable at a temperature of 25-30oC the solution with a high concentration of the diamine in the above molar ratio of polyetherpolyols and the prepolymer.

Comparative analysis of the proposed solutions with the prototype shows that in the present method, unlike known for dissolving 3,3'-dichloro-4,4'-diaminodiphenylmethane use except polyetherpolyols a prepolymer with terminal isocyanate groups, which chemically binds to part of 3,3'-dichloro-4,4 di aminophenylamino, and components - diamine, polyetherpolyols and the prepolymer are taken in a specific molar ratio, respectively: for two-functional polyetherpolyols(0,87-0,9) : (0,01-0,13) : 0,05; for trifunctional of polyetherpolyols(0,94-0,95) : (0,05-0,06) : 0,05 on 1 mol of the initial prepolymer.

This allows us to conclude that the proposed method has a "novelty" and meets the criterion of "inventive step".

Through the use of aggregate distinctive essential features of the proposed method allows to obtain a castable urethane elastomers with high strength properties at high viability of the reaction mass, which can, in turn, produce coatings of large shafts or other castings of high quality. This makes it possible to draw a conclusion on the conformity of the proposed technical solution the criterion of "useful effect".

Example 1. Charged to the reactor to reach 232.5 g (0.87 mol) of 3,3'-dichloro-4,4'-diaminodiphenylmethane and 133,3 g (0.13 mol) of polyoxyethyleneglycol. The mixture is heated to a temperature of 85-105oC and stirred until complete dissolution, then enter to 68.8 g (0.05 mole) of the prepolymer on the basis of polyoxyethyleneglycol and cooled to 25-30oC. the resulting solution is mixed under vacuum at room temperature for 15 min with 1377 g (1 mol) of the original polymer synthesized on the basis of polyoxyethyleneglycol and 2,4-toluylene diisocyanate, then pour samples for the determination of the viability of the reaction mass and strength properties of elastomers.

Example 2,3,4 are manufactured analogously to example 1 with the ratios shown in the table.

Example 5. Charged to the reactor 251 g (of 0.94 mol) of 3,3'-dichloro-4,4'-diaminodiphenylmethane and 192,0 (0.06 mol) of polyoxypropyleneglycol - Laprol 3203. The mixture is heated to a temperature of 85-105oC and stirred until complete dissolution, then enter to 68.8 g (0.05 mole) of the prepolymer on the basis of polyoxyethyleneglycol and 2,4-toluylene diisocyanate with a content of NCO - groups 6.1%, and stirred at a temperature of 95 - 100oC for 15 min and cooled to 25-30oC.

The resulting solution is mixed under vacuum at room temperature for 15 min with 1377 g source prepolymer synthesized on the basis of polyoxyethyleneglycol and 2,4-toluylene diisocyanate, then pour samples for the determination of the viability of the reaction mass and strength properties of elastomers.

The proposed method can be obtained urethane elastomers with similar properties, in which during preparation of the solution of diamine use other two - and trifunctionally the polyether polyols in the mixture of prepolymer on the basis of polyoxyethyleneglycol and 2,4-toluylene diisocyanate.

From the analysis of analogs and prototypes, as shown above, we can conclude that the highest strength properties of urethane elastomers obtained when using as the curing agent of the melt of the aromatic diamine in a pure form (viability 5-10 min).

Use as hardeners solutions diamine in various polyether polyols with terminal hydroxyl groups with the aim of improving the viability of the reaction mixture leads to the decrease of the strength characteristics, conditional stress at 100% strain and hardness of the resulting elastomers.

To preserve the high strength properties of urethane elastomers necessary to minimize the introduction of polyether polyols.

The proposed method allows to obtain a stable solution of the diamine in the small of siderites small amount of prepolymer - 0.05 mol per 1 mol of the initial prepolymer based polyoxyethyleneglycol and 2,4-toluylene diisocyanate, with a content of isocyanate groups of 6.1-7.2% and to obtain a urethane elastomers with high strength properties while maintaining high viability of the reaction mixture (see table).

The table shows the characteristics of urethane elastomers, obtained by the proposed method with a minimum content of polyetherpolyols and the prepolymer. Further reduction of the molar content of polyetherpolyols with terminal hydroxyl groups and prepolymer in the solution of the hardener outside of the claimed method is not desirable because it leads to bicrystalline diamine of the solution. Increasing the molar content of polyether polyols leads to deterioration of the strength properties of elastomers, and the increase in the content of the prepolymer is to increase the viscosity of the hardener solution.

On the basis of the proposed method of development of new grades of urethane elastomers of the type LOURE-90 high strength properties and high viability of the reaction mass, which enables to produce one large products for different purposes.

The way to receive is based hydroxyl-containing oligomer and 2,4-toluylene diisocyanate with a solution of 3,3'-dichloro-4,4'-diaminodiphenylmethane simple polyetherpolyols, characterized in that the prepolymer using a prepolymer based polyoxyethyleneglycol and 2,4-toluylene diisocyanate with a content of isocyanate groups of 6.1 to 7.2 mol.%, as a simple polyetherpolyols two or trifunctionally polyetherpolyols and solution pre-enter at 95 - 100oWith the prepolymer at a molar ratio of 3,3'-dichloro-4,4'-diamino-difenilmetana, polyetherpolyols and prepolymer equal(0,87 - 0,90): (0,10 - 0,13) : 0,05 in the case of the bifunctional polyester and(0,94 - 0,95) : (0,05 - 0,06) : 0,05 if trifunctional polyester, respectively, per 1 mol of the initial prepolymer entered after cooling the reaction mixture to 25 - 30oC.

 

 

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