CHEMCAD Tutorial Version 1.0 (Februar2012)
CHEMCAD Menüs
Hauptmenü
File
Open
Save as
E-Mail
Browse
Export
Edit
Copy Flowsheet to Clipboard
Select All
Find UnitOps
Find Streams
Edit UnitOp Symbols
View
Refresh Drawing
Zoom Options
Explorer
Palette
Messages
Status Bar
Toolbars
Toolsbars Command
Grid Visible
Snap to Grid
Change Gridsize
Show Page Bounds
Flowsheet Settings
Flowsheet Quickview
Refresh Data Boxes
Layers
Format
Engineering Units
Engineering Unit Selection
Starting Ids
UnitOP Box
All UnitOps
Select UnitOps
View Edit Group
Fill Pattern
Solid, Hollow, Horizontal etc.
Pen Style
Arrowheads
Color
Pen/Text
Fill Foreground
Fill Backgrund
Font
Align
Align to Grid
Aling Centers, Tops, Bottoms etc.
Import Bitmap
Add Stream Box
Add UnitOp Box
Add TP Box
Add Excel Range
Thermophysical
Component Database
View/Edit Database Component
View/Edit Simulations Component
Create New Component
Clone Component
Delete Component
Move Component
Manage Databases
Neutral File Import
List User Components
Component Property Regression
Database BIPs
Unifac Group Data
Database Electrolyte BIPs
Plot Properties
Select Components
Electrolytes
Electrolyte Settings
Electrolyte Regression
Add Electrolyte Reaction
Delete Electrolyte Reaction
Save Reactions to User DB
Override System Component
Pseudocomponent Curves
Solids
Identify Solid Components
Thermodynamics Wizard
Thermodynamic Settings
Edit BIPs
Regress BIPs
Import Cape-Open und View Cape-Open
Specifications
Select Streams
Feed Streams
Cut Streams
Copy Stream Data
Copy UnitOp Data
Specify Relative Humidity
Edit UnitOps
Select UnitOps
Add UnitOp Sequence Group
View/Edit Sequence Group
Remove Sequence Group
Select Cut Streams
Load Last Snap Shot
Run
Run Convergence
Run All
Run Selected UnitOps
Add UnitOp Sequence Group
View/Edit UnitOp Sequence Group
Remove UnitOp Sequence Group
Group 1
Recycles
Sensitivity Study
New Analysis
Optimization
Open
Data Reconciliation
Open
Report
Set Flowsheet Unit
Format Reports
Stream Compositions
Select Streams
Add Stream Group
View/Edit Stream Group
Remove Stream Group
All Streams
Feed Streams
Product Streams
Unit Streams
Group
Stream Properties
Select Properties
Select Streams
Add Stream Group
View/Edit Stream Group
Remove Stream Group
All Streams
Feed Streams
Product Streams
Unit Streams
Group
Particle Size Distribution
Pseudokomponent Curves
Unit Ops
Select UnitOps
Add UnitOps Sequence Group
View/Edit Sequence Group
Remove Sequence Group
Group
Spec Sheet
Select unit
All units
Distillation
Tray Compositions
Tray Properties
Column Mass Transfer (SCDS)
Dynamic Column History
Column Diagnosis
Topology
Thermodynamics
User Components Data
Mass and Energy Balances
Batch Results
Dynamics
Dynamic Column History
Kolonne Dynamic Stream History
Dynamic UnitOp History
Consolidated Report
New
Import
Global/Pool Reports
Simulation Reports
Plot
TPXY
Binary LLE
Binodal/Residue Curves
Residue Curves
Solid/Liquid Equilibrium
Stream Properties
Phase Envelopes
Composite Curves
Pseudocompenent Curves
Unit Plots
Column Profiles
Heat Curves
Plug Flow Reactor Profile
Pipe Profile
Controller Convergence
Der Controller iteriert in variablen Schritten vom Startwert zur Lösung. Er arbeitet nach dem Verfahren von Newton-Raphson, jedoch numerisch. Dynamic Plots
Batch Reactor / DVSL History
Dynamic Colum History
Dynamic UnitOp History
Stream History
User Specified File
Sizing
Distillation
Trays
Packing
Heat Exchangers
Shell & Tube
Plate
Double Pipe
Air Cooler
Vessel
Vessel LV Vessel
LVV Vessel
Piping
Orifice
Control Valve
Relief Device
Tools
Economics
Costing
Reaction Rate Regression
Excel Data Map
New Data Map
Edit Data Map
Execution Rules
Import
Execute Parser
Units Calculator
Simple Calculator
CO2 solid
Hydrates
Depressing
TOC/COD
Environmental Report
Visual Basic Editor
Macros
Options
Preferences
Licensing
Help
Help Topics
CHEMCAD Coach
Chemstations Website
Chemstations-Deutschland
Window
Cascade
Tile Horizontally
Tile Vertically
Split
Close All Charts
Close All Reports
Einführungsseminar
1: Flowsheet
Kreislauf-Gaswäsche
Kennzeichnung
2. Eng Units
3. Component
4. Thermodynamik-I
5. Streams
6. Unit Operation
Flash
Wärmeaustauscher
Pumpe
Mixer
Divider
7. Simulation
8. Kontrolle
Konvergenz
9. Report
ReportViewer
10. Zusammenfassung
Fortgeschrittenen Seminar
Themen
Phasengleichgewicht
Flash
Destillation
Thermodynamik-II
VLE
LLE
SLE
Enthalpie
Residuekurven
VBA-Funktionen
Unit Operations
Controller
Controller-Extra
Destillation
ShortCut
Beispiel-1
SCDS
Beispiel-1
Auslegung
Kosten
Masstransfer
Dynamisch
Optimierung
Feedboden
Seitenstrom
Rückflußverhältnis
Bodenzahl
Kosten
Trennblech
TOWR
TOWR PLUS
Dynamisch
PID-Controller
Beispiele
LevelModel
FeedChangeColm
Feststoff Units
Baghouse Filter
Zentrifuge
Crusher/Grinder
Kristallisation
Flash
LLE-Flash
Kompressor
Reaktoren
EREA
Kombiniert mit Gibbs
GIBBS
Verbrennung
KREA
Bioreaktor
REAC
BREAC
Rohrleitung
Subflowsheet-Meta
Turbine
Ventil
Wärmeaustauscher
User Unit
Excel-Unit-1
Mapping
VBA
ADDX-Unit
C-Unit (Calculator)
VBA-Unit-I
Pumpe
Mixer
Divider
Optimierung
Sensitivity Study
Datenbank
Standard Components
User Components
Funktionen
Eigene Stoffdatenfunktion
VBA-Stoffdaten
User Datenbank
Management
Job-User-Component
NRTL
Elektrolyt
Regression
Excel
Economics
Specsheets
Report
Excel Viewer
Elektrolyte
Tools
Hydratbildung
Konvergenz
Extras
Eigene Symbole
Eigene Menüs
Templates
Gruppen
Charts
Feststoffprozesse
Kostenschätzung
Reconciliation
Auslegung
Wärmeaustauscher
Beispiel-1
Interface
Excel-Mapping
VBA
VBA-Unit-II
XL-Chemcad-I
Excel-Unit-II
Theorie
Chemische Reaktoren
Kinetischer Reaktor KREA
Stoffdaten
Phasengleichgewicht
Thermodynamik-III
VLE-Phasengleichgewicht
Aktivitätskoeffizient
Fugazitätskoeffizient
Filme
Unit Operations
Controller
Destillation
SCDS
Literatur
Phasengleichgewichte
Destillation
Verfahrenstechnik
Wärmeaustauscher
Druckverlust
Stoffdaten
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CHEMCAD Tutorial Version 1.0 (Februar2012)
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