- (A) The corrosive and fouling fluid should be preferably routed through the tubes
- (B) The viscous fluid should be routed through the shell side
- (C) Lower flow rate fluid should be routed through the shell side
- (D) Higher pressure fluid stream should be routed through the shell side
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- (A) Filtering area & the pressure difference driving force
- (B) Viscosity of filtrate
- (C) Cake & filter medium resistance
- (D) Both
- (A) is more accurate in finding the number of equilibrium stages
- (B) accounts for the enthalpy changes in the process
- (C) Facilitates direct calculation of heat load on reboiler & condenser from, the diagram used in this method
- (D) All A,
- (A) 1
- (B) 2
- (C) 3
- (D) 3.5
- (A) Conical
- (B) Flat
- (C) Floating
- (D) Fixed
- (A) Decreases
- (B) Increases
- (C) Remain unaffected
- (D) May increase or decrease depending upon whether the fluid is Newtonian or non-Newtonian
- (A) Expansion joint
- (B) Changes in its direction
- (C) Change in the shape of pipeline
- (D) All
- (A) Less than
- (B) 1.25-1.50 times
- (C) 2.5 times
- (D) one-fourth of
- (A) Preventing the local overstressing of the shell around the opening
- (B) Reduction of discontinuity in shape at the junction
- (C) Making the joint leak proof
- (D) None of these
- (A) To increase the residence time of shell side fluid
- (B) To provide support to the tube bundle
- (C) To reduce the induced vibration in the tubes
- (D) To increase the tube side heat transfer co-efficient by inducing turbulence
