Saturated liquid ammonia is entering a 50 cm diameter 10-m long pipe at a steady 0.1 kg/s mass flow rate and a mean temperature of 0°C. It is exiting the pipe as saturated vapor at a mean temperature of 0°C. (a) What is the Reynolds number and flow regime at the beginning and at the end of the pipe? (b) If the surface temperature of the pipe can be assumed to be constant at 15°C in this section, what is the average convection coefficient of the ammonia flow? (a) 1343; 27075 (b) 553.6 W/m2K

Introduction to Chemical Engineering Thermodynamics
8th Edition
ISBN:9781259696527
Author:J.M. Smith Termodinamica en ingenieria quimica, Hendrick C Van Ness, Michael Abbott, Mark Swihart
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Saturated liquid ammonia is entering a 50 cm diameter 10-m long pipe at a steady 0.1 kg/s mass flow rate
and a mean temperature of 0°C. It is exiting the pipe as saturated vapor at a mean temperature of 0°C.
(a) What is the Reynolds number and flow regime at the beginning and at the end of the pipe?
(b) If the surface temperature of the pipe can be assumed to be constant at 15°C in this section, what
is the average convection coefficient of the ammonia flow?
(a) 1343; 27075
(b) 553.6 W/m2K
Transcribed Image Text:Saturated liquid ammonia is entering a 50 cm diameter 10-m long pipe at a steady 0.1 kg/s mass flow rate and a mean temperature of 0°C. It is exiting the pipe as saturated vapor at a mean temperature of 0°C. (a) What is the Reynolds number and flow regime at the beginning and at the end of the pipe? (b) If the surface temperature of the pipe can be assumed to be constant at 15°C in this section, what is the average convection coefficient of the ammonia flow? (a) 1343; 27075 (b) 553.6 W/m2K
Expert Solution
Step 1

Given:

Saturated liquid ammonia enters a pipe of diameter d = 0.5 m or 50 cm and L = 10 m. 

The mass flow rate of ammonia is m. = 0.1 kg/s and the mean temperature of Tin = Tout = 0oC

(a) The Reynolds number at the beginning can be calculated as follows:

Re = ρVdμRe = ρVdπ4dμ×π4d          (Multiplying and dividing by π4d)Re =  ρVπ4d2μ×π4dRe = ρVAμ×π4d      (A is the area)Re = 4m.μπd     (1)  (Since mass flow rate m. = ρVA)

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