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Abstract The thesis deals with the flow pattern of viscoelastic fluids through the plate model of the screw extruder. The calculation are carried out up to fluids of third order. The calculation showed that the,.velacity distribution . . for fluids of second order coinaides ~ith that of fluids of first order. The third order fluid leads to modification of -the velocity distributi9n. The distribution of third order veloc1~J matehes the experimental results in a better way than first order distributions. The extention of the present work to previd more realistic resul te to be compared with technical problems are discussed. |