Given that,
Chemical compound density, = 1400 kg/m3
Specific heat, C = 2500 J/kg/K
Volume, v = 3.5 m3
Cold storage temperature, Ti = 260 K
T = 420 K
Th = 500 K
Interior convection coefficient, hf = 8 kW/m2/K
Outside convection coefficient, hg = 2 kW/m2/K
Time, t =30min
Chemical reactors sometimes use batch processes to heat chemical compounds in a transient heating operation. Assume...
An 8 m3 batch of oil with specific heat of 2 kJ/(kg K) and density of 850kg/m3 is being heated in a steam-jacketed, agitated vessel with 1.5 m2 of heating surface. The convective heat-transfer coefficient on the oil side is 500W/(m2K), and 10,000 W/(m2K) on the steam side. If the steam temperature is 130°C and the initial temperature is 20 °C, estimate the oil temperature after 10 minutes.
PLEASE WRITE WITH CLEAR HANDWRITING & MENTION WHICH TABLE ARE USED. THANK YOU. Batch heating is a typical operation encountered in food processing. Consider a liquid food material that has to be heated in a highly agitated vessel that is fully insulated as shown in the diagram below: T. Cailed tubing Liquid Food TI Containment 1, Insulation The liquid food is to be heated by passing a hot fluid through a coiled thin walled tube with a surface area A....
A counter-flow heat exchanger is stated to have an overall heat transfer coefficient of 284 W/m2.K when operating at design and clean conditions. Hot fluid enters the tube side at 101°C and exits at 71°C, while cold fluid enters the shell side at 27°C and exits at 42°C. After a period of use, built-up scale in the heat exchanger gives a fouling factor of 0.0004 m2 K/W. The surface area is 93 m². Assume both hot and cold fluids have...