Ex Parte Brauer et al - Page 2




                Appeal No. 2005-0020                                                                              Page 2                  
                Application No. 09/572,225                                                                                                

                                                          INTRODUCTION                                                                    
                        The invention relates to a process for the continuous preparation of thermoplastically                            
                processable polyurethanes in a tubular mixer (stirred tubular reactor)(specification, p. 1, ll. 4-5                       
                and p. 2, ll. 22-24).  In the process, specified reactants are reacted in a tubular reactor equipped                      
                with a stirrer.  The stirrer is a monoaxially rotating stirrer having as mixing elements a member                         
                selected from the group consisting of beams, rods, anchors, grids, blades and propellers.                                 
                        Claim 1 is illustrative:                                                                                          
                        1. A continuous process for the preparation of thermoplastic, homogeneous polyurethane                            
                having improved softening properties comprising reacting substantially to completion, in a                                
                tubular reactor equipped with a stirrer at least one diisocyanate (A) with a mixture (B) containing                       
                        B1) 1 to 85 equivalent %, based on the isocyanate groups in (A) of at least one compound                          
                having on average at least 1.8 and at most 2.2 Zerewitinoff-active hydrogen atoms per molecule                            
                and a number average molecular weight of 450 to 5000 g/mol, and                                                           
                        B2) 15 to 99 equivalent %, based on the isocyanate groups in (A) of at least one chain                            
                lengthening agent having on average at least 1.8 and at most 2.2 Zerewitinoff-active hydrogen                             
                atoms per molecule and a molecular weight of 60 to 400 g/mol,                                                             
                wherein (A) and (B) are employed in a NCO:OH ratio of 0.9:1 to 1.1:1, said tubular reactor                                
                characterized in the absence of positively controlled conveyance therefrom and in that the ratio                          
                between the circumferential speed of said stirrer expressed in terms of meter/second and the                              
                throughput expressed in terms of g/second is greater than 0.03 meter/g, said reacting                                     
                substantially to completion amounting to conversion greater than 90%, based on starting                                   
                component (A) the said absence of positively controlled conveyance restricting said stirrer to a                          
                monoaxially rotating stirrer having as mixing elements a member selected from the group                                   
                consisting of beams, rods, anchors, grids, blades and propellers.                                                         
                        Claims 1-9 stand rejected under 35 U.S.C. § 112, ¶ 1 as lacking written descriptive                               
                support in the specification.  Specifically, the Examiner concludes that there is no support in the                       
                original specification for “the said absence of positively controlled conveyance restricting said                         







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