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Home Work: Convert TBP alve method Voliz Terp (°C) To = T10-AT1 T70=T50 + AT5 T90 = T70+ AT6 T90 = T95 + AT7 AT3=T50-T30 ATS=T70-T50 AT6 = T90-T70 AT7 = Tf-T90 " Where AT) = A₁(AT)B₁ AT1=T10-To AT2 = T30-T10 ASTM distillation curve F O 120 Index number i 1 More recently Daubert published a new method for distillation curves interconversion using the following equations: T50 = A4 (T50) B4 T30 = T50-AT3, T10 = T30-AT2 2 3 4 10 139 5 Where T and T the ASTM and TBP temperature respectively, both in F The subscripts o and f refer for initial and final temperature respectively Ai and Bi curve constant given in below table 6 30 155 A₁ 7.4012 4.9004 3.0305 0.8718 2.5282 50 3.0419 174 0.1180 for naphtha to 70 194 A4 9> B₁ 211 0.6024 0.7164 0.8008 1.0258 0.8200 0.7750 1.6606 95 Ва 232

Home Work: Convert TBP alve method Voliz Terp (°C) To = T10-AT1 T70=T50 + AT5 T90 = T70+ AT6 T90 = T95 + AT7 AT3=T50-T30 ATS=T70-T50 AT6 = T90-T70 AT7 = Tf-T90 " Where AT) = A₁(AT)B₁ AT1=T10-To AT2 = T30-T10 ASTM distillation curve F O 120 Index number i 1 More recently Daubert published a new method for distillation curves interconversion using the following equations: T50 = A4 (T50) B4 T30 = T50-AT3, T10 = T30-AT2 2 3 4 10 139 5 Where T and T the ASTM and TBP temperature respectively, both in F The subscripts o and f refer for initial and final temperature respectively Ai and Bi curve constant given in below table 6 30 155 A₁ 7.4012 4.9004 3.0305 0.8718 2.5282 50 3.0419 174 0.1180 for naphtha to 70 194 A4 9> B₁ 211 0.6024 0.7164 0.8008 1.0258 0.8200 0.7750 1.6606 95 Ва 232

Introduction to Chemical Engineering Thermodynamics
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
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Work: Home Bor naph tha to distillation Curne ASTM Convert TBP aivre me thod 여기 so 7. 35 10 232 174 194 139 155 Terp (°c) 120 More recently Daubert published a new method for distillation curves interconversion using the following equations: 2 T50 = A4(T50)#* T30 = T50 – AT3 T10 = T30 – AT2 To = T10 – AT, , T70= T50 + AT s T90 = T70 + AT, T90 = T95 + AT, Where T and T the ASTM and TBP temperature respectively, both in • F The subscripts o and f refer for initial and final temperature respectively Ai and Bi curve constant given in below table Index number i A, B, 1 7.4012 0.6024 | Where AT= A¿(AT,)B AT1 = T10 – To 2 4.9004 0.7164 AT2 = T30 – T10o AT 3 = T 50 – T 30 AT5 = T70 – T50 3 3.0305 0.8008 Be 4 0.8718 1.0258 AT, = T90 – T70 5 2.5282 0.8200 AT, = T¡ – T 90 6 3.0419 0.7750 0.1180 1.6606
Transcribed Image Text:Work: Home Bor naph tha to distillation Curne ASTM Convert TBP aivre me thod 여기 so 7. 35 10 232 174 194 139 155 Terp (°c) 120 More recently Daubert published a new method for distillation curves interconversion using the following equations: 2 T50 = A4(T50)#* T30 = T50 – AT3 T10 = T30 – AT2 To = T10 – AT, , T70= T50 + AT s T90 = T70 + AT, T90 = T95 + AT, Where T and T the ASTM and TBP temperature respectively, both in • F The subscripts o and f refer for initial and final temperature respectively Ai and Bi curve constant given in below table Index number i A, B, 1 7.4012 0.6024 | Where AT= A¿(AT,)B AT1 = T10 – To 2 4.9004 0.7164 AT2 = T30 – T10o AT 3 = T 50 – T 30 AT5 = T70 – T50 3 3.0305 0.8008 Be 4 0.8718 1.0258 AT, = T90 – T70 5 2.5282 0.8200 AT, = T¡ – T 90 6 3.0419 0.7750 0.1180 1.6606
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