AN INTRODUCTION TO ASPEN Plus AT CITY COLLEGE

Similar documents
TEACH YOURSELF THE BASICS OF ASPEN PLUS

Ammonia Synthesis with Aspen Plus V8.0

Aspen Dr. Ziad Abuelrub

Reactors. Reaction Classifications

Stoichiometric Reactor Simulation Robert P. Hesketh and Concetta LaMarca Chemical Engineering, Rowan University (Revised 4/8/09)

Principles of Chemical Engineering Processes

Introduction to Chemical Engineering Computing, 2 nd edition, Bruce A. Finlayson, Wiley (2012)

Pressure Swing Distillation with Aspen Plus V8.0

Polymers Plus. User Guide. With Aspen Plus 10 V O L U M E 2. Version POLYMER PROCESS MODELING. AspenTech

INTRODUCTION TO ASPEN PLUS SIMULATION

PRO/II PROCESS ENGINEERING: COMPREHENSIVE PROCESS SIMULATION

Esterification in a PFR with Aspen Plus V8.0

Esterification in CSTRs in Series with Aspen Plus V8.0

CHEMICAL ENGINEERING

POSITION R & D Officer M.Tech. No. of questions (Each question carries 1 mark) 1 Verbal Ability Quantitative Aptitude Test 34

Workshop 12 Simulators for Design Across the Curriculum ASEE Summer School, Colorado, August 2002

Thermodynamic Models & Physical Properties

Systems Engineering Spring Group Project #1: Process Flowsheeting Calculations for Acetic Anhydride Plant. Date: 2/25/00 Due: 3/3/00

Getting started with BatchReactor Example : Simulation of the Chlorotoluene chlorination

When using a chemical process simulator, the most

Ternary Maps for Liquid-Liquid Equilibrium Illustration with Aspen Plus V8.0

Incorporating Reality Into Process Simulation. Nathan Massey Chemstations, Inc. January 10, 2002

Aspen Polymers. Conceptual design and optimization of polymerization processes

Effect of Two-Liquid Phases on the Dynamic and the Control of Trayed Distillation Columns

DEVELOPMENT OF A CAPE-OPEN 1.0 SOCKET. Introduction

Figure 4-1: Pretreatment schematic

Aspen Plus PFR Reactors Tutorial using Styrene with Pressure Drop Considerations By Robert P. Hesketh and Concetta LaMarca Spring 2005

SIMULIS THERMODYNAMICS

INTRODUCTION TO CHEMICAL PROCESS SIMULATORS

Evaluation of the Dynamics of a Distillation Column with Two Liquid Phases

Optimization of the Sulfolane Extraction Plant Based on Modeling and Simulation

PRODUCTION OF ETHYLBENZENE FROM BENZENE AND ETHYLENE BY LIQUID-PHASE ALKYLATION USING ZEOLITE CATALYSTS. Aspen Model Documentation

CONTENTS. Notes to Students Acknowledgments ABOUT THE AUTHORS UNIT I FIRST AND SECOND LAWS 1

Comprehensive Process Simulation

Introduction to SuperPro Designer for Batch Processing Modelling

Adam G. Hawley Darin L. George. Southwest Research Institute 6220 Culebra Road San Antonio, TX 78238

Unit OperatiOn. Table 1: List of some unit operations

Aspen Plus. Getting Started Modeling Processes with Electrolytes

CAPE-OPEN and Simulis Thermodynamics enable you to use rigorous thermodynamics in MATLAB

Simulation and Optimization of Saponification of Ethyl Acetate in the Presence of Sodium Hydroxide in a Plug Flow Reactor Using Aspen Plus

Rigorous column simulation - SCDS

DME(10 TPD) Process Simulation Using Aspen Plus Release Dr. Jungho Cho, Professor Department of Chemical Engineering Dong Yang University

Integrated Knowledge Based System for Process Synthesis

ChemSep Case Book: Handling Missing Components

The Refined Electrolyte-NRTL Model applied to CO 2 -H 2 O-alkanolamine systems

,, Seong-Bo Kim,Hai-SongBae, and Jeong-Sik Han

Mass Transfer and Separation Processes

USE OF EQUATIONS OF STATE (EOS) SOFTWARE. Donald P. Mayeaux. President A+ Corporation, LLC Black Bayou Rd. Gonzales, LA USA

Rigorous calculation of LNG flow reliefs using the GERG-2004 equation of state

Separations and Reactors Design Project. Production of Allyl Chloride

Overview of Reacting Flow

Thermodynamics, Design, Simulation and Benchmarking of Biofuel Processes

Shortcut Distillation. Agung Ari Wibowo, S.T., M.Sc Politeknik Negeri Malang Malang - Indonesia

Dynamic Simulation of Reactor to Produce 1- Butene by Dimerization of Ethylene

Approximate Procedures for Simulation and Synthesis of Nonideal Separation Systems. Teresa do Rosário Senos Matias

Stoichiometric Reactor Module

REFERENCE TEXTBOOKS MATERIAL AND ENERGY BALANCE: THERMODYNAMICS: TRANSPORT: KINETICS AND REACTOR DESIGN:

SIMULATION ANALYSIS OF FULLY THERMALLY COUPLED DISTILLATION COLUMN

TOPIC: Conceptual Flowsheet for Production of Benzene from Toluene. Proposed Solution:

Aspen Plus Simulation of Saponification of Ethyl Acetate in the Presence of Sodium Hydroxide in a Plug Flow Reactor

INTRODUCTION TO CHEMICAL ENGINEERING COMPUTING

Dynamic simulation of a reactor to produce 1-Butene by dimerization of ethylene Anurag Choudhary, Avinash Shetty, Satish Oswal

Simulation of 1,3-butadiene extractive distillation process using N-methyl-2-pyrrolidone solvent

Aspen Plus. Aspen Plus Ammonia Model

A comparative study on the recovery of 1,2-dichloroethane and the removal of benzene contained in the byproducts of VCM process

Note: items marked with * you should be able to perform on a closed book exam. Chapter 10 Learning Objective Checklist

ECH 4224L Unit Operations Lab I Thin Film Evaporator. Introduction. Objective

FDE 211 Material & Energy Balances. Instructor: Dr. Ilgin Paker Yikici Fall 2015

Part Number: Aspen Physical Property System 11.1 September 2001

Distillation. Sep-tek. Ch.11 (continued) Distillation (Multistage with reflux) Sigurd Skogestad. Separation of liquid mixtures by repeated evaporation

Chemical Engineering 140. Chemical Process Analysis C.J. Radke Tentative Schedule Fall 2013

Supporting Information for. Sodium Hydroxide Production from Seawater Desalination Brine: Process Design and Energy efficiency

Aggregate Models based on Improved Group Methods for Simulation and Optimization of Distillation Systems

Inside VMG - January 2013 [News - Articles - Courses - Webinars] - Virtual Materials Group, Inc.

Simulation of Butyl Acetate and Methanol Production by Transesterification Reaction via Conventional Distillation Process

Process Systems Engineering

Chapter 4. Problem SM.7 Ethylbenzene/Styrene Column

Slide 1. A look into the CAPE-OPEN kitchen of COCO. Jasper van Baten, AmsterCHEM

WS Prediction of the carbon deposition in steam reforming unit (Equilibrium reaction calculation in Gibbs Reactor)

Heterogeneous Azeotropic Distillation Operational Policies and Control

Lecture 1: Orientation

Name of Course: B.Tech. (Chemical Technology/Leather Technology)

Optimization Through Simulation

Simulation of Electrolyte Processes: Status and Challenges

Simulation and Parametric Study of Urea Decomposition Section

Course Name: Thermodynamics for Chemical Engineers

DISTILLATION. Keywords: Phase Equilibrium, Isothermal Flash, Adiabatic Flash, Batch Distillation

4.3 CONCLUSION: HOW TO CHOOSE A MODEL The right questions Ionic liquids What is the property of interest?

ASIAN JOURNAL OF CHEMISTRY

MAGNETITE OXIDATION EXAMPLE

SOFTWARE INTELIGENT PACKAGE FOR PHASE EQULIBRIA (PHEQ) IN SYSTEMS APPLIED IN CHEMISTRY AND CHEMICAL ENGINEERING

Efficient and Effective Instruction in Process Simulation Across the Chemical Engineering Curriculum

PREFACE. Julian C. Smith Peter Harriott. xvii

Simulation of Molecular Distillation Process for Lactic Acid

Introduction to Polymerization Processes

Applied Thermodynamics for Marine Systems Prof. P. K. Das Department of Mechanical Engineering Indian Institute of Technology, Kharagpur

Determining Liquid Capacity 4 th Annual Pipeline Knowledge Retention Chris Sonneborn November 7, 2013

BOUNDARY VALUE DESIGN METHOD FOR COMPLEX DEMETHANIZER COLUMNS

DESIGN AND CONTROL OF BUTYL ACRYLATE REACTIVE DISTILLATION COLUMN SYSTEM. I-Lung Chien and Kai-Luen Zeng

Condensed Phase Ethanol Conversion to Higher Alcohols. Tyler L. Jordison, Carl T. Lira, and Dennis J. Miller

Transcription:

AN INTRODUCTION TO ASPEN Plus AT CITY COLLEGE Prepared by I. H. RINARD Department of Chemical Engineering November 1997 (Revised October 1999) ASPEN Plus provided by Aspen Technology, Inc. Cambridge, Massachusetts 10/18/99 ASPEN Introduction 1

WHAT IS ASPEN? A computer program for steady-state process simulation (a.k.a. process Flowsheeting) Developed for the simulation of Chemical & Petrochemical Processes Coal-based Processes Petroleum Refining Polymer Processes One of many commercially available flowsheeting programs such as PRO II (Simulation Sciences) HYSIM (Hyprotech) ChemCad (Chemstation) 10/18/99 ASPEN Introduction 2

HOW DOES ASPEN WORK? Basic unit is the BLOCK model Unit operations (Distillation Columns, Reactors, etc.) Related operations such as piping User assembles flowsheet model by selecting and connecting appropriate Block models and specifying Block model parameters ASPEN solves sequentially for output streams given input streams and Block model parameters 10/18/99 ASPEN Introduction 3

BLOCK MODEL Input Streams Output Streams Model Parameters Physical Properties 10/18/99 ASPEN Introduction 4

Process Flow Sheet St8 C-1 St7 P-1 St6 St9 St1 M-1 St3 St4 E-1 St5 R-1 V-1 St2 Item ASPEN # Name Model M-1: Feed Mixer MIXER R-1: Reactor RSTOIC E-1: Condenser HEATER V-1: Flash Drum FLASH2 C-1: Compressor COMPR P-1: Purge Point FSEP St10 10/18/99 ASPEN Introduction 5

MAJOR COMPONENTS OF ASPEN Unit operations (BLOCK) model library Physical properties system Physical properties models (density, enthalpy, VLE, etc.) Pure component and binary pair databases Estimation capability for missing values Flow sheet convergence capability for recycle processes Control capability (Design Specs) 10/18/99 ASPEN Introduction 6

USEFUL FEATURES IN ASPEN Sensitivity analysis Cost estimation and profitability evaluation Optimization Process flow diagram generation Physical properties data regression 10/18/99 ASPEN Introduction 7

ASPEN BLOCK MODEL LIBRARY I Mixers and Splitters MIXER - Adds two or more streams together FSPLIT - Splits a stream into two or more SEP - Separates a stream component by component Flashes and Heaters FLASH2 - Two outlet flash FLASH3 - Three outlet flash HEATER - Heater/cooler HEATX - Two stream heat exchanger MHEATX - Multistream heat exchanger DECANTER - Liquid-liquid decanter 10/18/99 ASPEN Introduction 8

ASPEN BLOCK MODEL LIBRARY II Reactors RSTOIC - Stoichiometric reactor RYIELD - Yield reactor REQUIL - Equilibrium reactor RGIBBS - Equilibrium reactor RCSTR - CST reactor (requires kinetic model) RPLUG - Plug flow reactor (requires kinetic model) RBATCH - Batch reactor (requires kinetic model) 10/18/99 ASPEN Introduction 9

ASPEN BLOCK MODEL LIBRARY III Separators DISTIL - Shortcut distillation design DISTWU - Shortcut distillation rating RADFRAC - Rigorous distillation EXTRACT - Rigorous liquid-liquid extraction RATEFRAC - Rate-based distillation* BATCHFRAC - Batch distillation * PETROFRAC - Rigorous distillation for petroleum * Requires special license 10/18/99 ASPEN Introduction 10

ASPEN BLOCK MODEL LIBRARY IV Solids Processing CYCLONE - cyclone separator VSCRUB - Venturi scrubber CRYSTALLIZER - Mixed suspension mixed product removal crystallizer CRUSHER - Solids crusher SCREEN - Solids separator FABL - Fabric filter HYCYC - Hydrocyclone CFUGE - Centrifuge FILTER - Rotary vacuum filter SWASH - Single-stage solids washer 10/18/99 ASPEN Introduction 11

ASPEN BLOCK MODEL LIBRARY V Fluid Movers COMPR - Compressor/turbine MCOMPR - Multistage compressor/turbine PUMP - Pump/hydraulic Piping PIPELINE - Multiple segment pipe PIPE - Single segment pipe VALVE - Valve 10/18/99 ASPEN Introduction 12

ASPEN PHYSICAL PROPERTIES SYSTEM I What is an Option Set? A collection of methods used by ASPEN to evaluate thermodynamic properties such as enthalpy, density, and K-values as well as transport properties such as viscosity Some available Option Sets / K-value Method IDEAL - Ideal gas/ Raoult s Law & Henry s Law RK-SOAVE - Redlich-Kwong-Soave EOS PENG-ROB - Peng-Robinson EOS WILSON - RK/Wilson NRTL UNIFAC UNIQUAC - RK/NRTL - RK/UNIFAC - RK/UNIQUAC 10/18/99 ASPEN Introduction 13

ASPEN PHYSICAL PROPERTIES SYSTEM II Databanks PURECOMP - parameters for 1550 (mostly organic) cpds INORGANIC - data for 2450 (mostly inorganic ) cpds AQUEOUS SOLIDS - data for 900 ionic species - data for 3314solid cpds COMBUST - special databank for high temperature, gas phase calculations (59 cpds and free radicals) 10/18/99 ASPEN Introduction 14

ASPEN PHYSICAL PROPERTIES SYSTEM III WHAT IF THE DATA IS NOT IN THE DATABANK? PROVIDE THE MISSING DATA - PROPS DATA Capability REGRESS RAW DATA - Data Regression Capability ESTIMATE THE MISSING DATA Pure Components VLE and LLE - UNIFAC COMPONENT NAMING AND FORMULAS [Cn1Hn2On3Nn4Othern5]-nx, nx for isomers Example: Acetaldehyde: C2H4O-1 Ethylene Oxide: C2H4O-2 10/18/99 ASPEN Introduction 15

USING ASPEN THREE STEPS 1) Use the Model Manager to specify the problem 2) Run the problem 3) Analyze and report the results MODEL MANAGER To start from a Sun station, type APLUS Select equipment BLOCK models - drag and drop on work area Click and connect BLOCK models with streams Pull down forms menus and fill out 10/18/99 ASPEN Introduction 16

ASPEN SPECIFICATION FORMS 1) TITLE - Specify title for current problem 2) COMPONENTS - Specify what chemical components are to be included in the simulation 3) PROPERTIES - Specify what Option Set (or Sets) is to be used 4) BLOCKS - Provide specification data for each block included in the simulation [one form per BLOCK] 5) STREAMS - Specify each stream entering the flow sheet from OSBL, also any important recycle streams. Must specify state, composition and flow rate of the stream. These forms are required. Other forms to invoke other ASPEN capabilities are optional. 10/18/99 ASPEN Introduction 17