Chapter:
                                                             The general relation between shear stress and velocity gradient of fluid can be written as:
 `tau=A ((du)/(dy))^n+B`
Where A , B and n are constants that depend upon  type of fluid and condition imposed on  flow. Comment  value of se constants so that  fluid may behave as:
- An ideal fluid
- A newtonian fluid
- A non newtonian fluid
Also indicate wher  fluid with  following characteristics is Newtonian or non-Newtonian.
- `tau=A*y+B` and `U=C_1+C_2*y+C_3*y^2` 
- `tau=A*y^(n (n-1))` and `U=C*y^n`
                                                       
                                                        
                                                        
                                                        - An ideal fluid
- A newtonian fluid
- A non newtonian fluid
- `tau=A*y+B` and `U=C_1+C_2*y+C_3*y^2`
- `tau=A*y^(n (n-1))` and `U=C*y^n`
Solution:
Given,
`tau=A ((du)/(dy))^n+B`
IDEAL FLUID:
Since an ideal fluid has zero viscosity (i.e, shear stress is always zero regardless of the motion of the fluid), we have,
`A=B=0`
A NEWTONIAN FLUID:
Since a newtonian fluid follows the newtons law of viscosity, `tau=mu*(du)/(dy)`, therefore compairing, we get,
`n=1`,
`A=mu`,
`B=0`
Air,water,kerosine etc behaves as Newtonian fluid under normal working conditions.
A NON-NEWTONIAN FLUID:
Depending upon the value of power index `n`, the non-Newtonian fluid are classified as:
- If `n>1` and B=0, Dilatent fluid. Example: sugar solution, aqueous suspension and printing ink. 
- If `n<1` and B=0, Pseudo-plastic fluid. Example: Blood, milk, liquid cement and clay. Show More
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