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/10 ton/hr. Ethanol at (T= 25 °C.P=28 psi) is feed to continuous reactor with presence of Acid Sulphuric catalyzer to produce 8 ton /hr. ethylene and water at (T= 35 °C.P = 30 psi). Distillation process then will be applied to separate ethylene-H2O mixture. The vapor product7 ton /hr. (top product) mole fraction of ethylene 99% at the conditions (T = 60 °C P= 30 psi) Ethylene as a top product is then condensate with condenser to perform liquid ethylene at the same conditions, Iton /hr., while the bottom product 99% water at the conditions (T= 40 °C ,P= 30 psi). Hydrogenation (10 ton /hr. hydrogen at (T= 54 °C.P= 30 psi) of ethylene applies another reactor with presence of Nickel catalyzer to produce 6 ton /hr. of ethane at (T=40 °C.P=20 psi) as a final product. Draw PFD (process topology and summary table including stream information) for these processes. CH₂CH₂OH H₂SO4 CH=CH,+H;O CH₂=CH₂+H₂ NI ► CH,CH,

/10 ton/hr. Ethanol at (T= 25 °C.P=28 psi) is feed to continuous reactor with presence of Acid Sulphuric catalyzer to produce 8 ton /hr. ethylene and water at (T= 35 °C.P = 30 psi). Distillation process then will be applied to separate ethylene-H2O mixture. The vapor product7 ton /hr. (top product) mole fraction of ethylene 99% at the conditions (T = 60 °C P= 30 psi) Ethylene as a top product is then condensate with condenser to perform liquid ethylene at the same conditions, Iton /hr., while the bottom product 99% water at the conditions (T= 40 °C ,P= 30 psi). Hydrogenation (10 ton /hr. hydrogen at (T= 54 °C.P= 30 psi) of ethylene applies another reactor with presence of Nickel catalyzer to produce 6 ton /hr. of ethane at (T=40 °C.P=20 psi) as a final product. Draw PFD (process topology and summary table including stream information) for these processes. CH₂CH₂OH H₂SO4 CH=CH,+H;O CH₂=CH₂+H₂ NI ► CH,CH,

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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1/10 ton/hr. Ethanol at (T= 25 °C.P= 28 psi) is feed to continuous reactor with presence of Acid Sulphuric catalyzer to produce 8 ton /hr. ethylene and water at (T= 35 °C,P = 30 psi). Distillation process then will be applied to separate ethylene-H2O mixture. The vapor product7 ton /hr. (top product) mole fraction of ethylene 99% at the conditions (T = 60 °C P = 30 psi) Ethylene as a top product is then condensate with condenser to perform liquid ethylene at the same conditions, 1ton /hr., while the bottom product 99% water at the conditions (T= 40 °C, P = 30 psi). Hydrogenation (10 ton /hr. hydrogen at (T= 54 °C .P = 30 psi) of ethylene applies another reactor with presence of Nickel catalyzer to produce 6 ton /hr. of ethane at (T= 40 °C,P= 20 psi) as a final product. Draw PFD (process topology and summary table including stream information) for these processes. CH₂CH₂OH H₂SO4 CH_=CH,+HO CH₂=CH₂+H₂ NI CHCH
Transcribed Image Text:1/10 ton/hr. Ethanol at (T= 25 °C.P= 28 psi) is feed to continuous reactor with presence of Acid Sulphuric catalyzer to produce 8 ton /hr. ethylene and water at (T= 35 °C,P = 30 psi). Distillation process then will be applied to separate ethylene-H2O mixture. The vapor product7 ton /hr. (top product) mole fraction of ethylene 99% at the conditions (T = 60 °C P = 30 psi) Ethylene as a top product is then condensate with condenser to perform liquid ethylene at the same conditions, 1ton /hr., while the bottom product 99% water at the conditions (T= 40 °C, P = 30 psi). Hydrogenation (10 ton /hr. hydrogen at (T= 54 °C .P = 30 psi) of ethylene applies another reactor with presence of Nickel catalyzer to produce 6 ton /hr. of ethane at (T= 40 °C,P= 20 psi) as a final product. Draw PFD (process topology and summary table including stream information) for these processes. CH₂CH₂OH H₂SO4 CH_=CH,+HO CH₂=CH₂+H₂ NI CHCH
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