A. Horizontal
B. Vertical
C. Inclined
D. Random
Chemical Heat Transfer
Chemical Heat Transfer
A. Equal to
B. More than
C. Less than
D. Either more or less than (depending upon the fluid)
A. Grashoff
B. Reynolds
C. Both ‘a’ & ‘b’
D. Prandtl & Grashoff
A. Existence of thermal boundary layer
B. Temperature gradient produced due to density difference
C. Buoyancy of the bubbles produced at active nucleation site
D. None of these
A. Increased steam economy
B. Decreased steam consumption
C. Both A. and B.
D. Increased capacity
A. Wall or skin friction
B. Form friction
C. Both A. and B.
D. Turbulent flow
A. U1 – U2
B. 1/U1 – 1/U2
C. 1/U2 – 1/U1
D. U2 – U1
A. 1.26 h1
B. 0.794 h1
C. 0.574 h1
D. 1.741 h1
A. (1/U) Vs. (1/v0.8)
B. (1/v0.8) Vs. U
C. v0.8 Vs . U
D. (1/U) Vs. (1/V)
A. 35.5
B. 43.75
C. 81.25
D. 48.25