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A dimensionally consistent relation for the volume `V` of a liquid of coefficiet of viscosity `eta` flowing per second through a tube of radius `r` and length `l` and having a pressure difference `p` across its end, is

A

`V=(piPr^(4))/(8etal)`

B

`V=(pieta)/(8Pr^(4))`

C

`V=(8Peta)/(pir^(4))`

D

`V=(piPeta)/(8r^(4))`

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To derive a dimensionally consistent relation for the volume \( V \) of a liquid flowing through a tube, we will use dimensional analysis. The parameters involved are the coefficient of viscosity \( \eta \), the radius \( r \), the length \( l \), and the pressure difference \( p \). ### Step-by-Step Solution: 1. **Identify the Parameters and Their Dimensions**: - Volume \( V \): The dimension of volume is \( [V] = L^3 \). - Coefficient of viscosity \( \eta \): The dimension is \( [\eta] = M L^{-1} T^{-1} \). - Radius \( r \): The dimension is \( [r] = L \). - Length \( l \): The dimension is \( [l] = L \). - Pressure \( p \): The dimension is \( [p] = M L^{-1} T^{-2} \). 2. **Formulate the Relation**: We assume a relation of the form: \[ V = K \cdot \eta^a \cdot r^b \cdot l^c \cdot p^d \] where \( K \) is a dimensionless constant. 3. **Write the Dimensions of Each Side**: The left-hand side (LHS) has dimensions: \[ [V] = L^3 T^{-1} \] The right-hand side (RHS) will be: \[ [\eta^a] = (M L^{-1} T^{-1})^a = M^a L^{-a} T^{-a} \] \[ [r^b] = L^b \] \[ [l^c] = L^c \] \[ [p^d] = (M L^{-1} T^{-2})^d = M^d L^{-d} T^{-2d} \] 4. **Combine the Dimensions on the RHS**: The dimensions of the RHS can be expressed as: \[ [V] = M^{a+d} L^{-a+b+c-d} T^{-a-2d} \] 5. **Set Up the Dimensional Equations**: For the dimensions to be consistent, we equate the dimensions from LHS and RHS: - For mass: \( a + d = 0 \) (1) - For length: \( -a + b + c - d = 3 \) (2) - For time: \( -a - 2d = -1 \) (3) 6. **Solve the Equations**: From equation (1), we have: \[ d = -a \] Substitute \( d \) into equation (3): \[ -a - 2(-a) = -1 \implies -a + 2a = -1 \implies a = -1 \] Then substituting \( a \) back into equation (1): \[ d = -(-1) = 1 \] 7. **Substitute \( a \) and \( d \) into Equation (2)**: \[ -(-1) + b + c - 1 = 3 \implies 1 + b + c - 1 = 3 \implies b + c = 3 \] 8. **Determine \( b \) and \( c \)**: We have \( b + c = 3 \). Since the options involve \( r^4 \) or \( r^{-4} \), we can assume: - If \( b = 4 \), then \( c = -1 \). 9. **Final Relation**: Thus, substituting \( a, b, c, d \) into our original relation gives: \[ V = K \cdot \eta^{-1} \cdot r^4 \cdot l^{-1} \cdot p^1 \] Simplifying, we get: \[ V = K \cdot \frac{p \cdot r^4}{\eta \cdot l} \] The constant \( K \) can be determined to be \( \frac{\pi}{8} \) based on empirical data, leading to: \[ V = \frac{\pi}{8} \cdot \frac{p \cdot r^4}{\eta \cdot l} \] ### Conclusion: The dimensionally consistent relation for the volume \( V \) of a liquid flowing through a tube is: \[ V = \frac{\pi}{8} \cdot \frac{p \cdot r^4}{\eta \cdot l} \]
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When a viscous liquid flows , adjacent layers oppose their relative motion by applying a viscous force given by F = - eta A (dv)/(dz) where , eta = coefficient of viscosity , A = surface area of adjacent layers in contact , (dv)/(dz) = velocity gradient Now , a viscous liquid having coefficient of viscosity eta is flowing through a fixed tube of length l and radius R under a pressure difference P between the two ends of the tube . Now consider a cylindrical vloume of liquid of radius r . Due to steady flow , net force on the liquid in cylindrical volume should be zero . - eta 2pirl (dv)/(dr) = Ppir^(2) - int _(v)^(0),dv = P/(2 eta l) int_(tau)^(R) rdr ( :' layer in contact with the tube is stationary ) v = v_(0) (1- (r^(2))/(R^(2))) , where v_(0) = (PR^(2))/(4nl) :. " " Q = (piPR^(4))/(8sta l) This is called Poisecuille's equation . The velocity of flow of liquid at r = R/2 is

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