Extrusion process for the preparation of polyurethane ureas

Claim 2

A process for the continuous preparation of polyurethane ureas by reacting, either all at one time or stepwise, a reaction mixture comprising: (A) one or more polyisocyanates; (B) one or more compounds having an average of at least 1.8 Zerewitinoff-active hydrogen atoms and a molecular weight of from 400 to 10,000; (C) water in a quantity of from 0.07 to 40% by weight, based on the sum of Zerewitinoff-active compounds (B), (C) and (D); optionally with (D) other compounds having one or more Zerewitinoff-active hydrogen atoms and having a molecular weight of from 32 to 400; and optionally (E) monoisocyanates; further characterized in that the equivalent ratio of component (B) to the sum of components (C) and (D) is from 5:1 to 1:30, the molar proportion of component (C) amounts to at least 5% of the sum of (C) and (D) and the equivalent ratio of isocyanate groups to all the Zerewitinoff-active hydrogen atoms, including water, is below 1.1:1, further characterized in that said reaction is carried out in hot screw extruders, comprising: (a) multishaft extruders with self-cleaning screws and kneading elements; (b) introducing components (A), (B) and optionally (D) and (E) into said hot screw extruder; (c) introducing component (C) into said screw-extruder, where the temperature in those extruders is between 120° and 280° C., thereby transferring component (C) into the gaseous phase; (d) adjusting pressure and temperature in the reaction zone of the extruders as to keep component C into the gaseous phase; (e) adjusting the temperature in the extrusion zone so as to subject the extrudate to a pressure of at least 10 bar.

Claim 3

A process for the continuous preparation of polyurethane ureas by reacting, either all at one time or stepwise, a reaction mixture comprising: (A') an isocyanate group-containing prepolymer obtained by prereacting (1) one or more polyisocyanates and (2) one or more compounds having an average of at least 1.8 Zerewitinoff-active hydrogen atoms and a molecular weight in the range of 400 to 10,000; (B) water in a quantity of from 0.07 to 40% by weight, based on the sum of Zerewitinoff-active compounds (A',2),(B) and (C); optionally with (C) other compounds having one or more Zerewitinoff-active hydrogen atoms and having a molecular weight of from 32 to 400; and optionally (D) monoisocyanates; further characterized in that the equivalent ratio of component (A') (2) to the sum of components (B) and (C) is from 5:1 to 1:30, the molar proportion of component (B) amounts to at least 5% of the sum of (B) and (C) and the equivalent ratio of isocyanate groups to all the Zerewitinoff-active hydrogen atoms, including water, is below 1.1:1, further characterized in that said reaction is carried out in hot screw extruders, comprising (a) multishaft extruders with self-cleaning screws and kneading elements; (b) introducing components (A'), (C) and optionally (D) into said hot screw extruders (c) introducing component (B) into said screw extruders, where the temperature in those extruders is between 120° and 280° C., thereby transferring component (B) into the gaseous phase; (d) adjusting pressure and temperature in the reaction zone as to keep component (B) in the gaseous phase; (e) adjusting the temperature in the extrusion zone so as to subject the extrudate to a pressure of at least 10 bar.

Claim 4

A process for the continuous preparation of polyurethane ureas by reacting, either all at one time or stepwise, a reaction mixture comprising: (A') an isocyanate group-containing prepolymer obtained by prereacting (1) one or more polyisocyanates and (2) one or more compounds having an average of at least 1.8 Zerewitinoff-active hydrogen atoms and a molecular weight in the range of 400 to 10,000; (B) water in a quantity of from 0.07 to 40% by weight, based on the sum of Zerewitinoff-active compounds (A',2),(B) and (C); optionally with (C) other compounds having one or more Zerewitinoff-active hydrogen atoms and having a molecular weight of from 32 to 400; and optionally (D) monoisocyanates; further characterized in that the equivalent ratio of component (A') (2) to the sum of components (B) and (C) is from 5:1 to 1:30, the molar proportion of component (B) amounts to at least 5% of the sum of (B) and (C) and the equivalent ratio of isocyanate groups to all the Zerewitinoff-active hydrogen atoms, including water, is below 1.1:1, further characterized in that said reaction is carried out in hot screw extruders, comprising (a) multishaft extruders with self-cleaning screws and kneading elements; (b) introducing components (A'), (C) and optionally (D) into said hot screw extruders (c) introducing component (B) into said screw extruders, where the temperature in those extruders is between 120° and 280° C., thereby transferring component (B) into the gaseous phase; (d) adjusting pressure and temperature in the reaction zone as to keep component (B) in the gaseous phase; (e) adjusting the temperature in the extrusion zone so as to subject the extrudate to a pressure of at least 10 bar.

Claim 5

A process as claimed in claim 1 or 2, wherein the reaction between isocyanate groups and water takes place at a temperature in the range of 170° to 270° C.

Claim 6

A process as claimed in claim 1 or 2, wherein said screw extruder is provided with one or more gas exhaust housings.

Claim 7

A process as claimed in claim 4, wherein said one or more exhaust gas housings are under excess pressure.

Claim 8

A process as claimed in claim 1 or 2, wherein said water is introduced into said screw extruder in a position downstream of said other starting materials, viewed in the direction of transport.

Claim 9

A process as claimed in claim 1 or 2, wherein said water is used in excess of the theoretically required quantity calculated from the excess of the isocyanate groups over Zerewitinoff-active hydrogen atoms of components (B) and (D).

Claim 10

A process as claimed in claim 1 or 2, wherein said water is in the form of water of crystallization.

Claim 11

A process as claimed in claim 1 or 2, wherein said water is in an adsorptively bound form.

Claim 12

A process as claimed in claim 1 or 2, wherein said polyurethane urea is prepared in the presence of one or more other thermoplasts.