Process for producing finished and/or irreversibly embossed microporous sheet structures

Claim 2

In a method of producing microporous sheet structure having the appearance of artificial leather by coagulation of a polyurethane solution in which a coagulatable polyurethane solution is coagulated, washed, and dried, and in which a finishing agent for making artificial leather is utilized for making a leather appearance, the improvement wherein the polyurethane solution is spread out flat such that it has a free upper surface and wherein said finishing agent for making artificial leather is applied to the free surface of the polyurethane solution which has been spread out flat and before coagulation thereof to achieve a leather appearance without a subsequent finishing step.

Claim 3

An improved method according to claim 1 wherein the sheet structure is embossed before drying.

Claim 4

An improved method according to claim 2 wherein the sheet structure is embossed during coagulation.

Claim 5

An improved method according to claim 2 wherein the sheet structure is embossed after coagulation.

Claim 6

An improved method according to claim 1 wherein said finishing agent is applied to said flat surface by applying thereto a further polyurethane solution containing a finishing agent for making artificial leather.

Claim 7

An improved method according to claim 5 wherein said leather finishing agent of said further polyurethane solution contains a coloring agent.

Claim 8

An improved method according to claim 5 wherein said leather finishing agent of said further polyurethane solution contains an agent imparting a leather-like smell.

Claim 9

An improved method according to claim 5 wherein said leather finishing agent of said further coagulatable polyurethane solution contains a material which produces characteristics affecting the handling quality of said artificial leather.

Claim 10

An improved process according to claim 1 wherein said polyurethane solution comprises an end solution in which a. an NCO preadduct is provided in a suitable solvent and then b. so much of the NCO preadduct solution is mixed continuously within a certain space of time, with constant measurement of the viscosity, into a previously prepared solution of a suitable solvent and hydrazine and/or hydrazine derivatives and/or diamines and/or polyols, it being necessary in the event of only two hydrogen atoms active according to Zerewitinow being present in these compounds to use in addition such a compound which contains at least three differently active hydrogen atoms according to Zerewitinow, until the viscosity is in a range in which even the addition of ever smaller amounts of NCO preadduct solution causes an ever greater increase in viscosity, until finally the viscosity has reached a value -- and the addition of the NCO preadduct solution must then be broken off at the latest -- at which the addition of a further very small amount of NCO preadduct solution would result in immediate gelling, the addition of the NCO preadduct solution being effected at such a rate that the end solution has a solids content between 15 and 35% by weight.

Claim 11

An improved process according to claim 9 wherein an NCO preadduct solution is used which has a solids content between 60 and 80% by weight.

Claim 12

An improved process according to claim 9 wherein the NCO preadduct in solution contains 1.5 to 5% of free isocyanate groups.

Claim 13

An improved process according to claim 9 wherein a solution containing hydrazines and/or dihydrazine compounds and/or diamines is used which contains the hydrazines and/or dihydrazine compounds and/or diamines in a concentration of 0.02 to 0.05 mol %.

Claim 14

An improved process according to claim 9 wherein the solvent used is a highly polar solvent, preferably an organic solvent, in particular dimethylformamide.

Claim 15

An improved process according to claim 9 wherein a hydrazine solution is used which is prepared from hydrazine hydrate and dimethylformamide.

Claim 16

An improved process according to claim 9 wherein a hydrazine solution is used and wherein the solutions are reacted at a temperature between 20° and 40° C, in particular between 25° and 35° C.

Claim 17

An improved process according to claim 9 wherein the hydrazines and/or dihydrazine compounds and/or diamines are used in a stoichiometric excess or deficiency with respect to the isocyanate groups present and, in the case of a deficiency, substances are added to the solution which contain at least two groups having active hydrogen atoms, these substances being used in excess.

Claim 18

An improved process according to claim 9 wherein substances having a cross-linking action, are dissolved in addition in the solution containing the hydrazines and/or dihydrazine compounds and/or diamines, and before this solution is used, at least one member selected from the group consisting of fillers, organic pigments, inorganic pigments, dyes, optical brighteners, UV absorbing agents, antioxidants and substances having a supplementary cross-linking action are added thereto.

Claim 19

An improved process according to claim 9 wherein the coagulating bath comprises water, and wherein the polyurethane solution which is spread out flat is introduced into the coagulating bath without previous gelling.