Ex Parte Bissen et al - Page 7




          Appeal No. 2003-0771                                                        
          Application No. 09/031,666                                                  


          for these differences, the examiner takes the position that it              
          would have been obvious to one of ordinary skill in the art “to             
          incorporate the capacity of the pump, nozzle and hose                       
          (interpreted as supply lines) as disclosed by Williams to the               
          device of Krynytzky et al. to combat large fires” (answer, page             
          4), and that it also would have been obvious “to incorporate the            
          third boom section, the third actuator assembly, and the third              
          pipe section of Ronan et al. to the device of Krynytzky et al. to           
          better articulate the nozzle” (answer, page 5), and that it                 
          further would have been obvious “to mount a tank and pump on the            
          chassis of Krynytzky et al. as taught by Thorton-Trump to                   
          eliminate the need for a separate pumper, therefore, enabling               
          independent operation of the fire fighting system of Krynytzky et           
          al.” (answer, page 5).  In addition, the examiner considers                 
          (answer, page 4) that operation of the above modified device of             
          Krynytzky would inherently result in turbulent flow of the                  
          quenching agent.                                                            



          quenching agent volumetric flow rate of about 5,000 gallons per             
          minute through the conveying pipeline,” and independent claim               
          17 calls for the step of operating the pump to pump the quenching           
          agent to the nozzle “at a pump discharge pressure of 150 pounds             
          per square inch and through the conveying pipeline at a turbulent           
          flow rate of at least about 3,000 gallons per minute.”                      
                                          7                                           





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