3. Use Fig. 1.5-1 to find the viscosity, expressed in mPa·s, of chloroform (CHC13) at 1207 °C and 108 atm. Use the following values for the critical constants: Tc = 536.6 K, Pc = 54.0 atm, V240 cm³/mol. 20 20 10 Liquid 8 1967 6 5 4 Reduced viscosity µ, µ/H 2 Dense gas P Pr= Pe 25 10 Two-phase region 5 1.0 2. 0.9 Critical 0.8 point 0.7 0.6 0.5 0.5 Low density limit 0.4 p=0.2 0.3 0.2 0.4 0.5 0.6 0.8 1.0 2 3 4 5 6 8 10 Reduced temperature T, = T/T, Fig. 1.5-1. Reduced viscosity H, H/H, as a function of reduced temperature for several values of the reduced pressure. [O. A. Uyehara and K. M. Watson, Nat. Petroleum News, Tech. Section, 36, 764 (Oct. 4, 1944); revised by K. M. Watson (1960). A large-scale version of this graph is available in O. A. Hougen, K. M. Watson, and R. A. Ragatz, C. P. P. Charts, Wiley, New York, 2nd edition (1960).]

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
Publisher:J.M. Smith Termodinamica en ingenieria quimica, Hendrick C Van Ness, Michael Abbott, Mark Swihart
Chapter1: Introduction
Section: Chapter Questions
Problem 1.1P
Question
3.
Use Fig. 1.5-1 to find the viscosity, expressed in mPa·s, of chloroform (CHC13) at
1207 °C and 108 atm. Use the following values for the critical constants: Tc = 536.6 K, Pc =
54.0 atm, V240 cm³/mol.
Transcribed Image Text:3. Use Fig. 1.5-1 to find the viscosity, expressed in mPa·s, of chloroform (CHC13) at 1207 °C and 108 atm. Use the following values for the critical constants: Tc = 536.6 K, Pc = 54.0 atm, V240 cm³/mol.
20
20
10
Liquid
8
1967
6
5
4
Reduced viscosity µ, µ/H
2
Dense gas
P
Pr=
Pe
25
10
Two-phase
region
5
1.0
2.
0.9
Critical
0.8
point
0.7
0.6
0.5
0.5
Low density limit
0.4 p=0.2
0.3
0.2
0.4 0.5 0.6 0.8 1.0
2 3 4 5 6 8 10
Reduced temperature T, = T/T,
Fig. 1.5-1. Reduced viscosity H, H/H, as a function of reduced temperature for several
values of the reduced pressure. [O. A. Uyehara and K. M. Watson, Nat. Petroleum News, Tech.
Section, 36, 764 (Oct. 4, 1944); revised by K. M. Watson (1960). A large-scale version of this
graph is available in O. A. Hougen, K. M. Watson, and R. A. Ragatz, C. P. P. Charts, Wiley,
New York, 2nd edition (1960).]
Transcribed Image Text:20 20 10 Liquid 8 1967 6 5 4 Reduced viscosity µ, µ/H 2 Dense gas P Pr= Pe 25 10 Two-phase region 5 1.0 2. 0.9 Critical 0.8 point 0.7 0.6 0.5 0.5 Low density limit 0.4 p=0.2 0.3 0.2 0.4 0.5 0.6 0.8 1.0 2 3 4 5 6 8 10 Reduced temperature T, = T/T, Fig. 1.5-1. Reduced viscosity H, H/H, as a function of reduced temperature for several values of the reduced pressure. [O. A. Uyehara and K. M. Watson, Nat. Petroleum News, Tech. Section, 36, 764 (Oct. 4, 1944); revised by K. M. Watson (1960). A large-scale version of this graph is available in O. A. Hougen, K. M. Watson, and R. A. Ragatz, C. P. P. Charts, Wiley, New York, 2nd edition (1960).]
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