SEPARATION SYSTEM CSTR C- 101 C- 102 PBR V- 102 C- 103.

Slides:

Advertisements

Similar presentations

Advertisements

Word Equations- State of the substance The reactants are the names of the substances that you begin with at the start of the reaction and the products.

Equipment Design and Costs for Separating Homogeneous Mixtures.

Structural Design and Separation Characteristic of Divided Wall Column by the Shortcut Method ● What is DWC ? -The DWC consists of one column in which.

STOY-KEE-AHM-EH-TREE. It‘s the study of amounts of substances that are involved in reactions.

How many moles of water will be produced when 8 grams of hydrogen gas react with the oxygen in the air? Episode 801.

Classification of Matter

CENG 221 Lecture 4. Multi-component Distillation (4.5 h)

Liquid-Liquid Equilibrium

Dividing wall column application

Separation Trains Azeotropes

Chapter 3 Distillation.

Separating Azeotropic Mixtures CHEN 4460 – Process Synthesis, Simulation and Optimization Dr. Mario Richard Eden Department of Chemical Engineering Auburn.

Group Members: Group Leader: Mohammad Al-Kashan Barjas Al-Otaibi Nasser Sohail Ahmad Boland Mutlaq Al-Shamery.

EB Plant EQUATE Petrochemical Company. Agenda EB Unit Description EB Plant Overview -Basic chemistry -Basic chemistry -Design of EB plant -Design of EB.

AC RGA Analyzers1 Multi-Purpose Gas Analysis. AC RGA Analyzers2 Refinery Gas Analysis Control specifications and purity of finished gas products: LPG,

Miscible or Immiscible

Multi-component Distillation Prepared by Dr

Material balance on single unit process

Multi-Comp. Distillation Design Short-Cut Method Example Problem

Approximate Methods for Multicomponent, Multistage Separations

Internal Column Balances Feed tray F V V L L Feed Equation: y = -{(L - L)/(V - V)}x + Fz f /(V-V) y = -(L f /V f )x + (F/V f )z f y = {q/(q-1)}x.

Propylene Oxide Production by ARCO Process Done By Fiasal Juhail.

SEQUENCING OF AZEOTROPIC DISTILLATION COLUMNS

Chemstations, Inc – Houston, TX – – Short Cut - Fenske-Underwood-Gilliland - Limited design, Rating Tower - Rigorous.

McCabe Thiele Graphical Equilibrium-Stage

Water phase changes constant Temperature remains __________

Introduction to Separation

Friday February 1, 2013 (Quiz 17). C 3 H 8 + O 2 æ CO 2 + H 2 O Bell Ringer Friday, What is the mole ratio of the reaction of propane gas (C 3.

Stoichiometry. What Is It? Branch of chemistry that shows the relationships among reactants and products in a chemical reaction Equations must be balanced.

Composition of constituents The composition of constituent of a mixture is not fix. Air is made up of a mixture of gases. There is ___ % nitrogen gas,

Cycles of Matter.  What is the function of the water cycle? It moves water from Earth's surface to the atmosphere and back.  What are the three processes.

Dealing with Impurities in Processes and Process Simulators

“Chemical Engineering Equilibrium Separations”

Relative Formula Mass expressed in grams

“Chemical Engineering Equilibrium Separations” Lectures Oct 2012.

Chapter 12 Notes. Information given by chemical equations 2 C 6 H 6 (l) + 15 O 2 (g)  12 CO 2 (g) + 6 H 2 O (g)  In this equation there are 2 molecules.

Thermodynamics of Separation Operations

Other Sources of Enthalpy Data Specific heats tabulated (see Appendix of thermodynamic textbook) and graphical data Riedel Equation  H n /RT n = 1.092(InP.

The Production of Ethanol from Syngas

Dr Saad Al-ShahraniChE 201: Introduction to Chemical Engineering  Separation operations are subject to the conservation of mass  Separation of components.

Solutions and Other Mixtures

Supervised By: Prof. M. A. FahimEng. Yusuf Ismail

Production of Ethanol from Synthesis Gas

Separation Trains S, S&L Chapt. 7. Simple Separation Unit Operations Flash Quench Liquid-liquid decantation Liquid-liquid Flash Crystallization Sublimation.

ORGANISM  Any living thing. 7 Characteristics of Living Things.

McCabe Thiele Part Two Today we will discuss:

Balancing Equations P + + = O + + = GCSE/A Level Chemistry.

S, S&L Chapt. 8 T &S Chapter 16 and 17

Noor Ahmad · Thomas Deskins · Lily Li · Shiv Patel

Aromatics Unit Revamp Kenning Engineering Dr. Leon Fan PhD.

Aspen Separation Unit Operations

Separation Columns (Distillation, Absorption and Extraction)

A Review of Separation Topics

Photosynthesis occurs in 2 stages

Terry A. Ring Chemical Engineering University of Utah

Underwood Equations – (L/D)min

7.5 – NOTES Molecular Formulas

Aspen Separation Unit Operations

SEQUENCING OF AZEOTROPIC DISTILLATION COLUMNS

Distillation Column – External Balance

Overall Review CHE 1008 Chapters 1-5, 6.4, 7, 9, 11, 12, 15.

Mass Balance- in Non-Reactive System 1 (Single unit)

Limiting Conditions – Reflux Ratios

MCD – Short-Cut Methods

Percentage Composition

7.3 – NOTES Molecular Formulas

Separation Columns (Distillation, Absorption and Extraction)

Mass Balance- in Non-Reactive System 1 (Single unit)

Presentation transcript:

SEPARATION SYSTEM CSTR C- 101 C- 102 PBR V- 102 C- 103

Column 1: Benzene Recovery (C-101) ComponentInlet (kg/hr) Distillate (kg/hr) Bottom (kg/hr) i-Butane i-Butene Butene n-Butane ,3-Butadiene Trans-2-Butene Cis-2-Butene Vinyl- cyclohexene Benzene Total  Column Operating Data Fenske Eq.Gilliland Eq. Nmin = 9.6 stagesN=22 stages  Mass Balance Underwood Eq. Rmin = R= Kirkbride Eq. Nr = 2 stagesNs=20 stages Number of stages Reflux ratio Feed tray location

Column 2: VCH Recovery (C-102) ComponentInlet (kg/hr) Distillate (kg/hr) Bottom (kg/hr) i-Butane i-Butene Butene n-Butane ,3-Butadiene Trans-2-Butene Cis-2-Butene Vinyl- cyclohexene Benzene Total  Column Operating Data Fenske Eq.Gilliland Eq. Nmin = 11.1 stagesN=23 stages  Mass Balance Underwood Eq. Rmin = 0.67R=1.0 Kirkbride Eq. Nr = 10 stagesNs=15 stages Number of stages Reflux ratio Feed tray location

3-Phase Separator: Decanter (V-102) ComponentInlet (kg/hr) Gas (kg/hr) Light Liquid (kg/hr) Heavy Liquid (kg/hr) Nitrogen Oxygen Carbon Dioxide Benzene Water Vinyl- cyclohexene Styrene Total  Mass Balance

Column 3: Styrene Purification (C-103) ComponentInlet (kg/hr) Distillate (kg/hr) Bottom (kg/hr) Nitrogen Oxygen Carbon Dioxide Benzene Water Vinyl- cyclohexene Styrene TBC Total  Column Operating Data Fenske Eq.Gilliland Eq. Nmin = 9.10 stagesN=29 stages  Mass Balance Underwood Eq. Rmin = R=8.126 Kirkbride Eq. Nr = 6 stagesNs=23 stages Number of stages Reflux ratio Feed tray location