Search
.Management Sciences
A. Steam
B. Condensate
C. Non-condensable
D. None of these
Related Mcqs:
- The overall heat transfer co-efficient for a shell and tube heat exchanger for clean surfaces is U0 = 400 W/m2.K. The fouling factor after one year of operation is found to be hd0 = 2000 W/m2.K. The overall heat transfer co-efficient at this time is _____________________?
- A. 1200 W/m2.K B. 894 W/m2.K C. 333 W/m2.K D. 287 W/m2.K...
- Indirect contact heat exchangers are preferred over direct contact heat exchangers, because_________________?
- A. Heat transfer co-efficient are high B. There is no risk of contamination C. There is no mist formation D. Cost of equipment is lower...
- A BTU/hr.ft.2 °F is equal to_________________?
- A. 1 kcal/hr. m2°C B. 4.88 kcal/hr. m.2°C C. 1 kcal/hr. m2.°K D. None of these...
- In case of a multipass shell and tube heat exchanger, the temperature drop in the fluid _______________?
- A. Is inversely proportional to the resistance across which the drop occurs B. And the wall are proportional to individual resistances C. And the wall is not related D. None of these...
- Heat transfer by ____________ may not necessarily require the presence of a medium?
- A. Conduction B. Natural convection C. Forced convection D. Radiation...
Recent Comments