Ex Parte ALTHAUSEN et al - Page 5




          Appeal No. 2001-1142                                                        
          Application No. 09/065,143                                                  


               the expansion phase of the mixture, after the mix head, and            
               allows for the progressive release of the blowing agent in             
               the reacting mass.  Accordingly, the four critical factors             
               can be varied to achieve the desired density rather than               
               having to be linked to a rigid set of parameters as was the            
               case with prior foam processes.  The speed and size of a               
               line or plant can be tailored to the needs of the foam                 
               manufacturer with speeds from 1 to 5 meters per minute, and            
               lengths as short as 20 meters or less, rather than the more            
               conventional length of about 100 meters.  This also permits            
               a smaller volume per hour of exhaust to be dealt with and              
               removed or scrubbed, simpler metering and plant fabrication,           
               foams made with CO2, a smaller volume of air to be                     
               conditioned, and very low densities down to about 14 kg/m3             
               or less.                                                               
                    . . . .  However, the pressure drop zone could be                 
               formed from other suitably shaped pressure-drop apertures              
               for flowing the mixture before frothing.  As is shown in               
               FIGS. 6 and 7, the discharge or gate bar 60 and 70,                    
               respectively could include a series of apertures of circular           
               (such as the spaced apart elongated, tubular holes or                  
               openings 74-78), oblong or rectangular shape (such as the              
               spaced apart slots 64-68), or a series of elongated, but               
               shorter, slots so long as the controlled conditions were               
               produced.  The slot or more precisely said pressure-drop               
               zone 17 has a restricted cross-sectional area sufficient to            
               cause a pressure reduction in the mixture emerging from the            
               chamber 21 during frothing, and a corresponding back                   
               pressure in the mixing device 11 for the purpose mentioned             
               above.                                                                 
                    . . . .                                                           
               The gate bar 60 could have the configuration shown in FIGS.            
               6 and 7.  In FIG. 6 the bar had a rectangular outer shape as           
               well as a rectangular cross-sectional inner chamber 62.  A             
               series of elongated slots, as are shown at 64, 66 and 68,              
               for example, could be used to provide the desired outlet               
               from the gate bar 60 and the desired pressure drop.  In FIG.           
               7 the gate bar 70 is provided with a circular cross-                   
               sectioned interior chamber 72 from which a series of tubular           

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