Copyright OLI Systems, Inc. All Rights reserved
|
|
|
- Adela Blake
- 5 years ago
- Views:
Transcription
1 Copyright 2006 OLI Systems, Inc. All Rights reserved The materials displayed here are provided to the lessees, selected individuals and agents of OLI systems, Inc. The material may not be duplicated or otherwise provided to any entity without the expressed permission of OLI Systems, Inc. 1
2 Part 01 2
3 OLI Programs The ESP package consists of four main programs. These are: OLI Databook ESP/Process OLI/Toolkit CSP/Stability 3
4 OLI Software OLI Databook ESP Process OLI Tool Kit CSP Stability Water Analyzer OLI Express ProChem ElectoChem DynaChem 4
5 ESP/Process Chemistry Model Process Build Process Analysis Process Summary Databanks User Added Chemistry Unit Ops Stream Block Results Calc Aids Output Reports 5
6 ESP/Toolkit Express Stream Definition New Streams Existing Streams Chemistry Model Calculate Databanks User Added Chemistry ScratchPad Survey 6
7 Model Generation The generation of Chemistry models is an central theme throughout the OLI software. The following is an overview of the necessary steps required to generate a model: 7
8 M o d e l G e n e r a tio n S e le c t P r o g r a m E n t e r O b je c t N a m e * E n te r C h e m N a m e is ty W / A M o d e l? N o B io M o d e l? N o S t d M o d e l? Y e Y e Y e E n te r In flo w N a m e s U s e A lte n t r y T e m p la t e s U s e A lte n t r y B io E n tr y T e m p la t e s P r iv. D B N o Y e U s e D B A ction M o d ify B io N o S e le c t S o lid s Y e M o d ify M o d e l R e v ie w M o d e l S e le c t P h a s e s E n t e r D B N a m e s Y e N o C h a n g e S o lid s G e n e r a t e D o n e 8
9 Unit Operations Unit operations are the core to ESP/Process. The following diagrams illustrate some of the features of each block. 9
10 Unit Operations 10
11 Unit Operations Mixer 11
12 Unit Operations Mixer Up to 7 inlet streams 1 outlet stream Calculations Available Adiabatic Isothermal Bubble point Temperature or Pressure Dew point Temperature or Pressure Vapor rate or fraction 12
13 Unit Operations Separator 13
14 Unit Operations Separator Up to 7 inlet streams 4 phase separations may be determined Incomplete separations (entrainment) can be specified for all phases All Mixer Block calculations are supported. 14
15 Unit Operations Absorber 15
16 Unit Operations Absorber Types Aqueous (standard) Aqueous with Mass Transfer Non-Aqueous Stages Theoretical Maximum = 50 Stage efficiencies (Muphree) may be specified 16
17 Unit Operations Absorber Mass Transfer coefficients may be specified Maximum of 10 inlet streams Condenser and/or Reboiler may be added Condenser types Total Partial Decanter Pump-arounds 17
18 Unit Operations Absorber Heat Exchanges on a stage Side Draws Specifications and Controllers Block Reports Composition on a stage Temperature, Pressure, Flowrate, Heat Duty on a stage Scaling Tendencies on a stage 18
19 Unit Operations Neutralizer 19
20 Unit Operations Neutralizer Normally used to set a stream ph Reagent stream (pictured at top of block) flowrate is varied to match the Set Point ph. Adiabatic Up to 7 inlet streams (not including the reagent stream) 1 outlet stream Reagent stream can not be from elsewhere in the process. 20
21 Unit Operations Activated Sludge Bioreactor Simple configuration 21
22 Unit Operations Activated Sludge Bioreactor Simple configuration Requires bioreaction chemistry model Adiabatic or Isothermal Bioreaction constants are adjustable Block Reports Substrate Utilization Heat Duty (Isothermal) Nutrient Requirements Concentrations Design Warnings 22
23 Unit Operations Controller (Feed Back) 23
24 Unit Operations Controller (Feed Back) Determines specified value in target stream Computes the difference between the value and the Set Point Adjusts a block parameter based on the difference. The block is upstream of the controller Possible specified values Temperature Pressure ph Flowrate Composition 24
25 Unit Operations Manipulate 25
26 Unit Operations Manipulate Types Flow Component Adjusts the flow or composition by multiplying the flow by a factor: Flow inlet * Factor = Flow outlet The factor is frequently adjusted by a controller 26
27 Summary In this section we discussed: How a chemistry model is created mathematically The components of the software and the architecture The Unit operations and a brief description of each block. 27
28 Part 2
29 Controllers/Recycles Consider the NEUTRAL1 process Mix 1 Sep 1 Neut 1 ph 9 29
30 Controllers/Recycles Neutralizer Blocks may not be suitable if: To control the ph you must adjust another upstream or downstream block. The set point may be an impossible case You need to control something other than ph 30
31 This may be an impossible ph Looks like this may be a constant ph 31
32 Solid NaHCO 3 is forming 32
33 33
34 Controllers/Recycles You can control ph Temperature Pressure Flow Concentration Oxidation/Reduction Potential 34
35 Controllers/Recycles Delete the neutralizer Mix 1 Sep 1 35
36 Controllers/Recycles Insert the Manipulator Mix 1 Sep 1 Manip 36
37 Controllers/Recycles Insert the new Neutralizer Mix Block Mix 1 Sep 1 Neut Manip 37
38 Controllers/Recycles Add the controller Mix 1 Sep 1 Neut Manip 38
39 Controllers/Recycles Adding the Recycle and additional blocks Mix 1 Sep 1 Neut Manip Tear 39
40 Part 2
41 Controllers/Recycles Consider the NEUTRAL1 process Mix 1 Sep 1 Neut 1 ph 9 41
42 Controllers/Recycles Neutralizer Blocks may not be suitable if: To control the ph you must adjust another upstream or downstream block. The set point may be an impossible case You need to control something other than ph 42
43 This may be an impossible ph Looks like this may be a constant ph 43
44 Solid NaHCO 3 is forming 44
45 45
46 Controllers/Recycles You can control ph Temperature Pressure Flow Concentration Oxidation/Reduction Potential 46
47 Controllers/Recycles Delete the neutralizer Mix 1 Sep 1 47
48 Controllers/Recycles Insert the Manipulator Mix 1 Sep 1 Manip 48
49 Controllers/Recycles Insert the new Neutralizer Mix Block Mix 1 Sep 1 Neut Manip 49
50 Controllers/Recycles Add the controller Mix 1 Sep 1 Neut Manip 50
51 Controllers/Recycles Adding the Recycle and additional blocks Mix 1 Sep 1 Neut Manip Tear 51
52 Part 2
53 Controllers/Recycles Consider the NEUTRAL1 process Mix 1 Sep 1 Neut 1 ph 9 53
54 Controllers/Recycles Neutralizer Blocks may not be suitable if: To control the ph you must adjust another upstream or downstream block. The set point may be an impossible case You need to control something other than ph 54
55 This may be an impossible ph Looks like this may be a constant ph 55
56 Solid NaHCO 3 is forming 56
57 57
58 Controllers/Recycles You can control ph Temperature Pressure Flow Concentration Oxidation/Reduction Potential 58
59 Controllers/Recycles Delete the neutralizer Mix 1 Sep 1 59
60 Controllers/Recycles Insert the Manipulator Mix 1 Sep 1 Manip 60
61 Controllers/Recycles Insert the new Neutralizer Mix Block Mix 1 Sep 1 Neut Manip 61
62 Controllers/Recycles Add the controller Mix 1 Sep 1 Neut Manip 62
63 Controllers/Recycles Adding the Recycle and additional blocks Mix 1 Sep 1 Neut Manip Tear 63
64 Part 2
65 Controllers/Recycles Consider the NEUTRAL1 process Mix 1 Sep 1 Neut 1 ph 9 65
66 Controllers/Recycles Neutralizer Blocks may not be suitable if: To control the ph you must adjust another upstream or downstream block. The set point may be an impossible case You need to control something other than ph 66
67 This may be an impossible ph Looks like this may be a constant ph 67
68 Solid NaHCO 3 is forming 68
69 69
70 Controllers/Recycles You can control ph Temperature Pressure Flow Concentration Oxidation/Reduction Potential 70
71 Controllers/Recycles Delete the neutralizer Mix 1 Sep 1 71
72 Controllers/Recycles Insert the Manipulator Mix 1 Sep 1 Manip 72
73 Controllers/Recycles Insert the new Neutralizer Mix Block Mix 1 Sep 1 Neut Manip 73
74 Controllers/Recycles Add the controller Mix 1 Sep 1 Neut Manip 74
75 Controllers/Recycles Adding the Recycle and additional blocks Mix 1 Sep 1 Neut Manip Tear 75
Version 6.7. OLI Systems, Inc. A Guide to Using ESP
A Guide to Using ESP Version 6.7 OLI Systems, Inc. A Guide to Using ESP Contents i This manual was authored by OLI Systems, Inc. The underlying software is the product of over 30 years of devotion by the
A Guide to Using. ESP/Process. OLI Systems, Inc.
A Guide to Using ESP/Process OLI Systems, Inc. ph Dedication: To Robinson, Stokes, Pitzer, Meisner, Bromley, Helgeson, Debye, Huckel and many others, you have blazed a trail such that we may follow. Get
Pressure Swing Distillation with Aspen Plus V8.0
Pressure Swing Distillation with Aspen Plus V8.0 1. Lesson Objectives Aspen Plus property analysis RadFrac distillation modeling Design Specs NQ Curves Tear streams Understand and overcome azeotrope Select
Getting started with BatchReactor Example : Simulation of the Chlorotoluene chlorination
Getting started with BatchReactor Example : Simulation of the Chlorotoluene chlorination 2011 ProSim S.A. All rights reserved. Introduction This document presents the different steps to follow in order
OLI Tips #80 Reaction Kinetics and OLI (Revised November 8, 2017)
Think Simulation OLI Tips #80 Reaction Kinetics and OLI (Revised November 8, 2017) Reaction Kinetics Overview... 3 New Thermodynamic Framework... 3 Variable Names relating to Activities... 3 Building Standard
A Guide to Using. OLI Analyzer Studio. Including Studio ScaleChem. Version 9.1. OLI Systems, Inc.
A Guide to Using OLI Analyzer Studio Including Studio ScaleChem Version 9.1 OLI Systems, Inc. Copyright 2014 OLI Systems, Inc. All rights reserved. The enclosed materials are provided to the lessees, selected
Shortcut Distillation. Agung Ari Wibowo, S.T., M.Sc Politeknik Negeri Malang Malang - Indonesia
Shortcut Distillation Agung Ari Wibowo, S.T., M.Sc Politeknik Negeri Malang Malang - Indonesia The use of separation column in HYSYS The column utilities in HYSYS can be used to model a wide variety of
Figure 4-1: Pretreatment schematic
GAS TREATMENT The pretreatment process consists of four main stages. First, CO 2 and H 2 S removal stage which is constructed to assure that CO 2 would not exceed 50 ppm in the natural gas feed. If the
Stoichiometric Reactor Simulation Robert P. Hesketh and Concetta LaMarca Chemical Engineering, Rowan University (Revised 4/8/09)
Stoichiometric Reactor Simulation Robert P. Hesketh and Concetta LaMarca Chemical Engineering, Rowan University (Revised 4/8/09) In this session you will learn how to create a stoichiometric reactor model
DISTILLATION. Keywords: Phase Equilibrium, Isothermal Flash, Adiabatic Flash, Batch Distillation
25 DISTILLATION Keywords: Phase Equilibrium, Isothermal Flash, Adiabatic Flash, Batch Distillation Distillation refers to the physical separation of a mixture into two or more fractions that have different
TEACH YOURSELF THE BASICS OF ASPEN PLUS
TEACH YOURSELF THE BASICS OF ASPEN PLUS TEACH YOURSELF THE BASICS OF ASPEN PLUS RALPH SCHEFFLAN Chemical Engineering and Materials Science Department Stevens Institute of Technology A JOHN WILEY & SONS,
USE OF EQUATIONS OF STATE (EOS) SOFTWARE. Donald P. Mayeaux. President A+ Corporation, LLC Black Bayou Rd. Gonzales, LA USA
USE OF EQUATIONS OF STATE (EOS) SOFTWARE Donald P. Mayeaux President A+ Corporation, LLC 41041 Black Bayou Rd. Gonzales, LA USA Introduction Proper sample conditioning is essential to providing a representative
ESP FLOWSHEET SIMULATION APPLICATION BRIEF Chlor-Alkali Simulation
ESP FLOWSHEET SIMULATION APPLICATION BRIEF Chlor-Alkali Simulation Revised April 10, 2012 1 The anode in an electrochemical cell is the strongest oxidizer known, as it is fully capable of taking an electron
Process Unit Control System Design
Process Unit Control System Design 1. Introduction 2. Influence of process design 3. Control degrees of freedom 4. Selection of control system variables 5. Process safety Introduction Control system requirements»
Mass Transfer Operations I Prof. Bishnupada Mandal Department of Chemical Engineering Indian Institute of Technology, Guwahati
Mass Transfer Operations I Prof. Bishnupada Mandal Department of Chemical Engineering Indian Institute of Technology, Guwahati Module - 5 Distillation Lecture - 5 Fractional Distillation Welcome to the
Back to the Basics: NeSSI or Not NeSSI the Basics Are the Same
Falcon Analytical makers of the... Back to the Basics: NeSSI or Not NeSSI the Basics Are the Same IFPAC 2013 John Crandall, President Falcon Analytical Dr. Brian Rohrback, President Infometrix Mike Cost,
Determining the Ionic Dew Point
OLI Systems, Inc. Determining the Ionic Dew Point Amine Surveys in Refinery Overhead Chemistry using OLI Studio Rasika Nimkar May 5, 2017 Copyright 2017 OLI Systems, Inc. All rights reserved. The enclosed
Full Furnace Simulations and Optimization with COILSIM1D
Full Furnace Simulations and Optimization with COILSIM1D Kevin M. Van Geem 1 Alexander J. Vervust 1 Ismaël Amghizar 1 Andrés E. Muñoz G. 2 Guy B. Marin 1 1 Laboratory for Chemical Technology, Ghent University
PFR with inter stage cooling: Example 8.6, with some modifications
PFR with inter stage cooling: Example 8.6, with some modifications Consider the following liquid phase elementary reaction: A B. It is an exothermic reaction with H = -2 kcal/mol. The feed is pure A, at
Cork Institute of Technology. Autumn 2005 CE 2.7 Separation Process & Particle Technology (Time: 3 Hours) Section A
Cork Institute of Technology Bachelor of Engineering (Honours) in Chemical and Process Engineering Stage 2 (Bachelor of Engineering in Chemical and Process Engineering Stage 2) (NFQ Level 8) Autumn 2005
INTEGRATION OF DESIGN AND CONTROL FOR ENERGY INTEGRATED DISTILLATION
INTEGRATION OF DESIGN AND CONTROL FOR ENERGY INTEGRATED DISTILLATION Hongwen Li, Rafiqul Gani, Sten Bay Jørgensen CAPEC, Department of Chemical Engineering Technical University of Denmark, Lyngby, Denmark
INDUSTRIAL EXPERIENCE WITH HYBRID DISTILLATION PERVAPORATION OR VAPOR PERMEATION APPLICATIONS
INDUSTRIAL EXPERIENCE WITH HYBRID DISTILLATION PERVAPORATION OR VAPOR PERMEATION APPLICATIONS Mario Roza, Eva Maus Sulzer Chemtech AG, Winterthur, Switzerland; E-mails: mario.roza@sulzer.com, eva.maus@sulzer.com
Effect of Two-Liquid Phases on the Dynamic and the Control of Trayed Distillation Columns
Effect of Two-Liquid Phases on the Dynamic and the Control of Trayed Distillation Columns Gardênia Cordeiro, Karoline Brito, Brenda Guedes, Luis Vasconcelos, Romildo Brito Federal University of Campina
A First Course on Kinetics and Reaction Engineering Unit 19. Analysis of Batch Reactors
Unit 19. Analysis of Batch Reactors Overview As noted in Unit 18, batch reactor processing often follows an operational protocol that involves sequential steps much like a cooking recipe. In general, each
Heterogeneous Azeotropic Distillation Operational Policies and Control
Heterogeneous Azeotropic Distillation Operational Policies and Control Claudia J. G. Vasconcelos * and Maria Regina Wolf-Maciel State University of Campinas, School of Chemical Engineering, Campinas/SP,
DESIGN AND CONTROL OF BUTYL ACRYLATE REACTIVE DISTILLATION COLUMN SYSTEM. I-Lung Chien and Kai-Luen Zeng
DESIGN AND CONTROL OF BUTYL ACRYLATE REACTIVE DISTILLATION COLUMN SYSTEM I-Lung Chien and Kai-Luen Zeng Department of Chemical Engineering, National Taiwan University of Science and Technology, Taipei
Chemical Engineering 3P04 Process Control Tutorial # 1 Learning goals
Chemical Engineering 3P04 Process Control Tutorial # 1 Learning goals 1. Sensor Principles with the flow sensor example 2. The typical manipulated variable: flow through a conduit Sensors: We need them
Chapter 2 Introduction to Aqueous Speciation
Chapter 2 Introduction to Aqueous Speciation Overview It is our belief that the predictive modeling of aqueous systems requires that the system be fully speciated. This allows for smoother extrapolation
(1) This reaction mechanism includes several undesired side reactions that produce toluene and benzene:
HYSYS Multiple Reactions - Styrene Prepared by Robert P. Hesketh Spring 005 Styrene Reactor System You have been studying how to use HYSYS using the example of a Styrene reactor system. In this session
Aggregate Models based on Improved Group Methods for Simulation and Optimization of Distillation Systems
Aggregate Models based on Improved Group Methods for Simulation and Optimization of Distillation Systems Ravindra S. Kamath 1, Ignacio E. Grossmann 1,*, and Lorenz T. Biegler 1 1 Chemical Engineering Department,
TOPIC: Conceptual Flowsheet for Production of Benzene from Toluene. Proposed Solution:
Norwegian University of Science and Technology Course: Energy and Process Department of Energy and Process Engineering No.: TEP 4230 Trondheim, 17.09.04, T. Gundersen Part: Production Systems Task: 5 Year:
Vapor-liquid Separation Process MULTICOMPONENT DISTILLATION
Vapor-liquid Separation Process MULTICOMPONENT DISTILLATION Outline: Introduction to multicomponent distillation Phase Equilibria in Multicomponent Distillation (Pg. 737) Bubble-point and dew-point calculation
Dynamic Simulation of Reactor to Produce 1- Butene by Dimerization of Ethylene
International Journal of Scientific & Engineering Research, Volume 3, Issue 6, June-2012 1 Dynamic Simulation of Reactor to Produce 1- Butene by Dimerization of Ethylene Anurag Choudhary, Avinash Shetty,
Evaluation of the Dynamics of a Distillation Column with Two Liquid Phases
A publication of 2029 CHEMICAL ENGINEERING TRANSACTIONS VOL. 32, 2013 Chief Editors: Sauro Pierucci, Jiří J. Klemeš Copyright 2013, AIDIC Servizi S.r.l., ISBN 978-88-95608-23-5; ISSN 1974-9791 The Italian
A First Course on Kinetics and Reaction Engineering Unit 22. Analysis of Steady State CSTRs
Unit 22. Analysis of Steady State CSRs Overview Reaction engineering involves constructing an accurate mathematical model of a real world reactor and then using that model to perform an engineering task
Availability and Irreversibility
Availability and Irreversibility 1.0 Overview A critical application of thermodynamics is finding the maximum amount of work that can be extracted from a given energy resource. This calculation forms the
Process Dynamics, Operations, and Control Lecture Notes 2
Chapter. Dynamic system.45 Process Dynamics, Operations, and Control. Context In this chapter, we define the term 'system' and how it relates to 'process' and 'control'. We will also show how a simple
Vapour Absorption Refrigeration Systems Based On Ammonia- Water Pair Nagendra M CBM Engineer, Hindusthan Zink.Ltd The specific objectives of this lesson are to: 1. Introduce ammonia-water based vapour
Control Loop Investigations
Control Loop Investigations Peter Thomas Control Specialists Ltd ExperTune User Conference Austin Texas April 2007 www.controlspecialists.co.uk Control Loop Investigations Bridging the gap between Industrial
AN INTRODUCTION TO ASPEN Plus AT CITY COLLEGE
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
ENGR Thermodynamics
ENGR 224 - hermodynamics #1 - Diagram for a Cascade VCR Cycle (21 ts) Baratuci Final 13-Jun-11 On a full sheet of paper, construct a complete Diagram for the cascade cascade vapor-compression refrigeration
Heat Integration - Introduction
Heat Integration - Introduction Sub-Topics Design of Heat Exchanger Networks Selection of Utilities Ø Consumption and Production Correct Integration Ø Distillation and Evaporation Ø Heat Pumps Ø Turbines
Plant Design LECTURE 8: REBOILER CIRCUIT DESIGN. Daniel R. Lewin Department of Chemical Engineering Technion, Haifa, Israel
054410 Plant Design LECTURE 8: REBOILER CIRCUIT DESIGN Daniel R. Lewin Department of Chemical Engineering Technion, Haifa, Israel Ref: Kern, R. Thermosyphon Reboiler Piping Simplified, Hydrocarbon Processing,
Chapter 4. Problem SM.7 Ethylbenzene/Styrene Column
Background Chapter 4. Problem SM.7 Ethylbenzene/Styrene Column In Problem SM.6 of the HYSYS manual, a modified form of successive substitution, called the Wegstein method, was used to close the material
INTRODUCTION: Shell and tube heat exchangers are one of the most common equipment found in all plants. How it works?
HEAT EXCHANGERS 1 INTRODUCTION: Shell and tube heat exchangers are one of the most common equipment found in all plants How it works? 2 WHAT ARE THEY USED FOR? Classification according to service. Heat
Systems Engineering Spring Group Project #1: Process Flowsheeting Calculations for Acetic Anhydride Plant. Date: 2/25/00 Due: 3/3/00
10.551 Systems Engineering Spring 2000 Group Project #1: Process Flowsheeting Calculations for Acetic Anhydride Plant Date: 2/25/00 Due: 3/3/00 c Paul I. Barton, 14th February 2000 At our Nowhere City
Ways to Improve the Energy Efficiency of AN Solution Plants
Ways to Improve the Energy Efficiency of AN Solution Plants by Axel Erben Uhde GmbH Dortmund, Germany Prepared for Presentation at NITROGEN 2009 International Conference Rome, Italy 22-25 February 2009
OLI Simulation Conference 2010
OLI Simulation Conference 2010 Advances in OLI Simulation: Examples Wet Flue Gas Desulfurization and Amine Gas Sweetening Think Simulation! Harnessing the power of the OLI Engine James Berthold OLI Systems,
COMPARISON OF MEASURED AND ANALYTICAL PERFORMANCE OF SHELL-AND-TUBE HEAT EXCHANGERS COOLING AND HEATING SUPERCRITICAL CARBON DIOXIDE
The 4th International Symposium - Supercritical CO Power Cycles September 9-10, 014, Pittsburgh, Pennsylvania COMPARISON OF MEASURED AND ANALYTICAL PERFORMANCE OF SHELL-AND-TUBE HEAT EXCHANGERS COOLING
Process Classification
Process Classification Before writing a material balance (MB) you must first identify the type of process in question. Batch no material (mass) is transferred into or out of the system over the time period
STRUCTURAL ANALYSIS OF A WESTFALL 2800 MIXER, BETA = 0.8 GFS R1. By Kimbal A. Hall, PE. Submitted to: WESTFALL MANUFACTURING COMPANY
STRUCTURAL ANALYSIS OF A WESTFALL 2800 MIXER, BETA = 0.8 GFS-411519-1R1 By Kimbal A. Hall, PE Submitted to: WESTFALL MANUFACTURING COMPANY OCTOBER 2011 ALDEN RESEARCH LABORATORY, INC. 30 Shrewsbury Street
Energy and Energy Balances
Energy and Energy Balances help us account for the total energy required for a process to run Minimizing wasted energy is crucial in Energy, like mass, is. This is the Components of Total Energy energy
Nitrogen Oxide Closed System
Present study is the result of Development of Nitrogen Oxide Closed System in the Future Reprocessing Process entrusted to Japan Nuclear Fuel Limited by the Ministry of Education, Culture, Sports, Science
Microdetermination of phosphorus using the SPECTRAmax PLUS microplate spectrophotometer: choice of microplate, cuvette or test tube assay formats
Application Note 24 Microdetermination of phosphorus using the SPECTRAmax PLUS microplate spectrophotometer: choice of microplate, cuvette or test tube assay formats INTRODUCTION Most spectrophotometric
This immunoassay kit allows for the in vitro quantitative determination of Aflatoxin M1 concentrations in milk, milk power.
Aflatoxin M1 (AFM1) ELISA Kit This immunoassay kit allows for the in vitro quantitative determination of Aflatoxin M1 concentrations in milk, milk power. This package insert must be read in its entirety
Approximate Methods Fenske-Underwood-Gilliland (FUG) Method Selection of Two Key Components
Lecture 3. Approximate Multicomponent Methods () [Ch. 9] Approximate Methods Fenske-Underwood-Gilliland (FUG) Method Selection of Two Key Components Column Operating Pressure Fenske Equation for Minimum
Twin-Screw Food Extruder: A Multivariable Case Study for a Process Control Course
Twin-Screw Food Extruder: A Multivariable Case Study for a Process Control Course Process Control Course Overview Case Studies Realistic Industrial Problems Motivating to Students Integrate Techniques
Simulation of Electrolyte Processes: Status and Challenges
Simulation of Electrolyte Processes: Status and Challenges Paul M Mathias and Chau-Chyun Chen Aspen Technology, Inc. 12 March 2002 AIChE Spring 2002 Meeting AIChE 2002 Spring Meeting. Summary Opportunities/needs
THE PROCESS SIMULATION COURSE THE CULMINATION OF CORE UNDERGRADUATE COURSEWORK IN CHEMICAL ENGINEERING
THE PROCESS SIMULATION COURSE THE CULMINATION OF CORE UNDERGRADUATE COURSEWORK IN CHEMICAL ENGINEERING Mordechai Shacham, Ben-Gurion University, Beer-Sheva, Israel Michael B. Cutlip, University of Connecticut,
Simulation of Ethanol Dehydration Using Cyclohexane as an Entrainer
Simulation of Ethanol Dehydration Using Cyclohexane as an Entrainer 2013 년 9 월 23 일 ( 월 ) 공주대학교화학공학부조정호 Limit of Distillation by Azeotrope 1.0 Ethanol / Water System Distillation range is restricted by
CHEMICAL ENGINEERING LABORATORY CHEG 4137W/4139W. Reaction Kinetics Saponification of Isopropyl Acetate with Sodium Hydroxide
CHEMICAL ENGINEERING LABORATORY CHEG 4137W/4139W Reaction Kinetics Saponification of Isopropyl Acetate with Sodium Hydroxide Objective: The purpose of this experiment is to examine and determine the reaction
Introduction to SuperPro Designer for Batch Processing Modelling
Introduction to SuperPro Designer for Batch Processing Modelling Session outline Getting started SuperPro Designer (SPD) interface Flowsheet drawing and editing Unit procedures initialisation Simulation
Modeling and Simulation of Distillation + Pervaporation Hybrid Unit: Study of IPA - Water Separation
International Journal of ChemTech Research CODEN (USA): IJCRGG, ISSN: 0974-4290, ISSN(Online):2455-9555 Vol.10 No.5, pp 190-196, 2017 Modeling and Simulation of Distillation + Pervaporation Hybrid Unit:
Integrated Knowledge Based System for Process Synthesis
17 th European Symposium on Computer Aided Process Engineering ESCAPE17 V. Plesu and P.S. Agachi (Editors) 2007 Elsevier B.V. All rights reserved. 1 Integrated Knowledge Based System for Process Synthesis
Name: Discussion Section:
CBE 141: Chemical Engineering Thermodynamics, Spring 2017, UC Berkeley Midterm 2 FORM A March 23, 2017 Time: 80 minutes, closed-book and closed-notes, one-sided 8 ½ x 11 equation sheet allowed Please show
Chemical Process Design / Diseño de Procesos Químicos
Chemical Process Design / Diseño de Procesos Químicos Topic 4.7. Flash Javier R. Viguri Fuente Eva Cifrian Bemposta Department of Chemistry and Process & Resource Engineering GER Green Engineering and
ChemSep Tutorial: Distillation with Hypothetical Components
ChemSep Tutorial: Distillation with Hypothetical Components Harry Kooijman and Ross Taylor Here we use ChemSep to solve a complex multicomponent distillation problem presented in a paper entitled Multistage
BOUNDARY VALUE DESIGN METHOD FOR COMPLEX DEMETHANIZER COLUMNS
Distillation Absorption 2010 A.B. de Haan, H. Kooijman and A. Górak (Editors) All rights reserved by authors as per DA2010 copyright notice BOUNDARY AUE DESIGN METHOD FOR COMPEX DEMETHANIZER COUMNS Muneeb
Aflatoxin M1 (AFM1) ELISA Kit
Aflatoxin M1 (AFM1) ELISA Kit Catalog Number. CSB-EL027236 This immunoassay kit allows for the in vitro quantitative determination of Aflatoxin M1 concentrations in milk, milk power. This package insert
Simulation of a Thermo-Acoustic Refrigerator
Simulation of a Thermo-Acoustic Refrigerator Sohaib Ahmed 1, Abdul Rehman 1, Ammad Fareed 1, Syed Muhammad Sabih ul Haque 1, Ali Muhammad Hadi 1 1 National University of Sciences and Technology (NUST),
Effect of the Temperature in the Decanter on Total Annual Cost of the Separation Process for Binary Heterogeneous Azeotropic Mixture
1603 A publication of CHEMICAL ENGINEERING TRANSACTIONS VOL. 61, 2017 Guest Editors: Petar S Varbanov, Rongxin Su, Hon Loong Lam, Xia Liu, Jiří J Klemeš Copyright 2017, AIDIC Servizi S.r.l. ISBN 978-88-95608-51-8;
COMPUTER-AIDED HAZOP OF BATCH PROCESSES
COMPUTER-AIDED HAZOP OF BATCH PROCESSES Paul W.H. Chung and Steve A. McCoy Department of Computer Science, Loughborough University, Loughborough, Leicestershire LE11 3TU; UK; email: p.w.h.chung@lboro.ac.uk
Introduction to System Dynamics
SE1 Prof. Davide Manca Politecnico di Milano Dynamics and Control of Chemical Processes Solution to Lab #1 Introduction to System Dynamics Davide Manca Dynamics and Control of Chemical Processes Master
Mass Transfer Operations I Prof. Bishnupada Mandal Department of Chemical Engineering Indian Institute of Technology, Guwahati
Mass Transfer Operations I Prof. Bishnupada Mandal Department of Chemical Engineering Indian Institute of Technology, Guwahati Module - 4 Absorption Lecture - 4 Packed Tower Design Part - 3 Welcome to
Development of Dynamic Models. Chapter 2. Illustrative Example: A Blending Process
Development of Dynamic Models Illustrative Example: A Blending Process An unsteady-state mass balance for the blending system: rate of accumulation rate of rate of = of mass in the tank mass in mass out
Water & Wastewater Mixing (WWM)
Water & Wastewater Mixing (WWM) Steve Bungay October 2011 BHR Group offer Research Consultancy Product development in the field of Water, Environment and Power (WEP) With a multi-disciplinary team covering
Chapter 10. Vapor/Liquid Equilibrium: Introduction
Chapter 10 Vapor/Liquid Equilibrium: Introduction Preceding chapters have dealt largely with pure substances or with constant-composition mixtures. e.g., air. However, composition changes are the desired
Thermodynamics: An Engineering Approach Seventh Edition Yunus A. Cengel, Michael A. Boles McGraw-Hill, Chapter 7 ENTROPY
Thermodynamics: An Engineering Approach Seventh Edition Yunus A. Cengel, Michael A. Boles McGraw-Hill, 2011 Chapter 7 ENTROPY Copyright The McGraw-Hill Companies, Inc. Permission required for reproduction
Energy Conversion in the Peltier Device
Laboratory exercise 4 Energy Conversion in the Peltier Device Preface The purpose of this exercise is to become familiar with the Peltier effect. Students will observe Peltier device working as a heat
Dynamic simulation of a reactor to produce 1-Butene by dimerization of ethylene Anurag Choudhary, Avinash Shetty, Satish Oswal
Dynamic simulation of a reactor to produce 1-Butene by dimerization of ethylene Anurag Choudhary, Avinash Shetty, Satish Oswal Abstract The aim of this work was to develop dynamic simulation model for
University School of Chemical Technology
University School of Chemical Technology Guru Gobind Singh Indraprastha University Syllabus of Examination B.Tech/M.Tech Dual Degree (Chemical Engineering) (7 th Semester) (w.e.f. August 2004 Batch) Page
Micro-Channel Water Cooled Single Bar Diode Laser (QCW)
Micro-Channel Water Cooled Single Bar Diode Laser (QCW) MCC09 Features Long lifetime Low smile High power Narrow spectrum Applications Pumping Scientific research Industry Device Dimension (mm) This structure
BERMAD Irrigation. BIC2000 Weather Station SYSTEM GUIDE VERSIONS : BIC ; PC 4.90
BIC2000 Weather Station SYSTEM GUIDE VERSIONS : BIC2000 3.92; PC 4.90 CONTENTS 1. SYSTEM OVERVIEW 3 2. WEATHER STATION SETUP 4 2.1 ISS AND CONSOLE SETUP 4 2. RF RTU SYSTEM SETUP 5 2.2 BIC2000 WEATHER STATION
A Definition for Plantwide Controllability. Process Flexibility
A Definition for Plantwide Controllability Surya Kiran Chodavarapu and Alex Zheng Department of Chemical Engineering University of Massachusetts Amherst, MA 01003 Abstract Chemical process synthesis typically
MODA. Modelling data documenting one simulation. NewSOL energy storage tank
MODA Modelling data documenting one simulation NewSOL energy storage tank Metadata for these elements are to be elaborated over time Purpose of this document: Definition of a data organisation that is
ME 2322 Thermodynamics I PRE-LECTURE Lesson 23 Complete the items below Name:
Lesson 23 1. (10 pt) Write the equation for the thermal efficiency of a Carnot heat engine below: T η = T 1 L H 2. (10 pt) Can the thermal efficiency of an actual engine ever exceed that of an equivalent
ENTROPY. Chapter 7. Mehmet Kanoglu. Thermodynamics: An Engineering Approach, 6 th Edition. Yunus A. Cengel, Michael A. Boles.
Thermodynamics: An Engineering Approach, 6 th Edition Yunus A. Cengel, Michael A. Boles McGraw-Hill, 2008 Chapter 7 ENTROPY Mehmet Kanoglu Copyright The McGraw-Hill Companies, Inc. Permission required
Name: Discussion Section:
CBE 141: Chemical Engineering Thermodynamics, Spring 2017, UC Berkeley Midterm 2 FORM B March 23, 2017 Time: 80 minutes, closed-book and closed-notes, one-sided 8 ½ x 11 equation sheet allowed lease show
Numerical Simulation on Flow and Heat Transfer in Oscillating Heat Pipes
10th IHPS, Taipei, Taiwan, Nov. 6-9, 11 Numerical Simulation on Flow and Heat Transfer in Oscillating Heat Pipes S.F. Wang a,*, Z.R. Lin a, Z.Y. Lee b, and L.W. Zhang b a Key Laboratory of Enhanced Heat
Continuous Flow Reactions. From idea to production size scale up in 3 steps
Continuous Flow Reactions From idea to production size scale up in 3 steps PIN NL Spring Session 13 04 2017 13 4 2017 PIN NL Spring Session 1 Topics Introduction Flowlink Continuous Flow Reactions What
External Forced Convection. Copyright The McGraw-Hill Companies, Inc. Permission required for reproduction or display.
External Forced Convection Copyright The McGraw-Hill Companies, Inc. Permission required for reproduction or display. Drag and Heat Transfer in External flow Fluid flow over solid bodies is responsible
All rights reserved. Armando B. Corripio, PhD, PE Flash Distillation Flash Drum Variables and Specifications... 2
Flash Distillation All rights reserved. Armando B. Corripio, PhD, PE. 2013 Contents Flash Distillation... 1 1 Flash Drum Variables and Specifications... 2 2 Flash Drum Balances and Equations... 4 2.1 Equilibrium
Distillation. This is often given as the definition of relative volatility, it can be calculated directly from vapor-liquid equilibrium data.
Distillation Distillation may be defined as the separation of the components of a liquid mixture by a process involving partial vaporization. The vapor evolved is usually recovered by condensation. Volatility
Reactors. Reaction Classifications
Reactors Reactions are usually the heart of the chemical processes in which relatively cheap raw materials are converted to more economically favorable products. In other cases, reactions play essential
A novel framework for simultaneous separation process and product design
Chemical Engineering and Processing 43 (2004) 595 608 A novel framework for simultaneous separation process and product design M.R. Eden a, S.B. Jørgensen a, R. Gani a,, M.M. El-Halwagi b a CAPEC, Department
Dynamics and Control of Energy Integrated Distillation Column Networks
200 American Control Conference Marriott Waterfront, Baltimore, MD, USA June 30-July 02, 200 ThA4.4 Dynamics and Control of Energy Integrated Distillation Column Networks Sujit S. Jogwar and Prodromos
Lecture 1: Basics Concepts
National Technical University of Athens School of Chemical Engineering Department II: Process Analysis and Plant Design Lecture 1: Basics Concepts Instructor: Α. Kokossis Laboratory teaching staff: Α.
DME(10 TPD) Process Simulation Using Aspen Plus Release Dr. Jungho Cho, Professor Department of Chemical Engineering Dong Yang University
DME(10 TPD) Process Simulation Using Aspen Plus Release 12.1 Dr. Jungho Cho, Professor Department of Chemical Engineering Dong Yang University Overall Flowsheet for DME Production Unit 18 TO FLARE 17 DA-103
Thermodynamics: An Engineering Approach Seventh Edition in SI Units Yunus A. Cengel, Michael A. Boles McGraw-Hill, 2011.
Thermodynamics: An Engineering Approach Seventh Edition in SI Units Yunus A. Cengel, Michael A. Boles McGraw-Hill, 2011 Chapter 7 ENTROPY Mehmet Kanoglu University of Gaziantep Copyright The McGraw-Hill
Micro Volume QuEChERS kit
225-37872 Sep. 2018 Small Capacity Pretreatment Kit Micro Volume QuEChERS kit Instruction Manual Read this manual thoroughly before you use the product. Keep this manual for future reference. This page