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adjusting the temperature of the stream. For an overview of Solubility features, see Solubility. Example Project: For examples of the use of the solubility function

equilibrium calculations. It can use database files (CST files) generated using the FactSage family of products. It permits the calculation of complex, multicomponent

reports. Examples of calculations that may be used are: Ratio of two species or elements, Flow of particular ions, such as Ferric or Ferrous, Flow of a species

straight out of the 'Product' outlet; No material will flow out of the 'Vapour' outlet; The pressure of the outlet streams will be the pressure of the input

convergence speed of large networks; Adding user defined property calculations or species information calculations; Adding calculations using PGM or MP files;

SysCAD in the Examples folder, demonstrates the use of this model in a SysCAD project. This Falling Film Evaporator model can be included as part of a flash

} }[/math] where Q - Rate of Heat Transfer m - Mass flow of the stream Hin - Enthalpy of entering stream Hout - Enthalpy of leaving stream Using the stream

equilibrium calculations, please see Vapour Liquid Equilibrium (VLE) for more information. Example 1 - Entering BPE data into the Species Database Example 2 -

phase flash calculations are handled in SysCAD. Any solids that may be in the slurry stream entering the unit are ignored in the flash calculations, but the

phase flash calculations are handled in SysCAD. Any solids that may be in the slurry stream entering the unit are ignored in the flash calculations, but the

Mass Fraction, MFi and Density Calculation Examples. The user may view the corrected density of a solution consisting of ONLY the solvent and the solute

need only enter a single Cp equation and the range for that equation. The form of the equation can be any of those shown below. The forms of the equations

information required for Mass and Energy balance. See Model Examples for enthalpy calculation Examples. Unit Type: BaroCond - The first tab page in the access

user-specified calculations must exist to allow mapping of the aqueous and organic values. Please see example 2 on how to set up user calculations. The model

for calculating the pH of a solution. However, since SysCAD does NOT include calculations for buffering, this is an estimate of the pH only. SysCAD uses

PHREEQCResults tab - This tab displays the key results of the calculations. Input tab - This tab displays a summary of the mapped Input stream as PHREEQC species.

OLIResults tab - This tab displays the key results of the calculations. Input tab - This tab displays a summary of the mapped Input stream as OLI species. Output

information required for Mass and Energy balance. See Model Examples for enthalpy calculation Examples. Unit Type: FlashTank1 - The first tab page in the access

PHREEQCResults tab - This tab displays the key results of the calculations. Input tab - This tab displays a summary of the mapped Input stream as PHREEQC species.

} }[/math] where Q - Rate of Heat Transfer m - Mass flow of the stream Hin - Enthalpy of entering stream Hout - Enthalpy of leaving stream Using the stream

and perform calculations. OLIResults tab - This tab displays the key results of the calculations. Input tab - This tab displays a summary of the Input stream

information required for Mass and Energy balance. See Model Examples for enthalpy calculation Examples. Unit Type: Evaporator - The first tab page in the access

PHREEQCResults tab - This tab displays the key results of the calculations. Input tab - This tab displays a summary of the Input stream. Output tab - This tab displays

OLIResults tab - This tab displays the key results of the calculations. Input tab - This tab displays a summary of the mapped Input stream as OLI species. Output

Results. This tab displays the key results of the calculations. Input tab - This tab displays a summary of the mapped Input stream as AQSol species. Output

AQSolResults tab - This tab displays the key results of the calculations. Input tab - This tab displays a summary of the mapped Input stream as AQSol species. Output

recover of overrides of tolerance settings of individual variables in a Tear Block. Improved save and recover of Tear state. Fixed bug for use of Tol.Strategy

and perform calculations. AQSolResults tab - This tab displays the key results of the calculations. Input tab - This tab displays a summary of the Input

PHREEQCResults tab - This tab displays the key results of the calculations. Input tab - This tab displays a summary of the mapped Input stream as PHREEQC species.

information required for Mass and Energy balance. See Model Examples for enthalpy calculation Examples. Unit Type: PipingSystem - The first tab page in the access

latest version of SysCAD 139. For users using older versions of SysCAD, please use Paste Special - Text in MS Excel to ensure the copied example syntax is converted

OLIResults tab - This tab displays the key results of the calculations. Input tab - This tab displays a summary of the Input stream. Output tab - This tab displays

} }[/math] where Q - Rate of Heat Transfer m - Mass flow of the stream Hin - Enthalpy of entering stream Hout - Enthalpy of leaving stream Using the stream

ChemAppResults tab - This tab displays the key results of the calculations. Input tab - This tab displays a summary of the mapped Input stream as ChemApp species.

displays the key results of the calculations. Input tab - Optional tab, only visible if Rxns.Option = TCE. This tab displays a summary of the mapped Input stream

PHREEQCResults tab - This tab displays the key results of the calculations. Input tab - This tab displays a summary of the Input stream. Output tab - This tab displays

fraction of liquid in the concentrate stream. Note: the material entering the unit via the 'Conc Launder' inlet is NOT included in these calculations, but

PHREEQCResults tab - This tab displays the key results of the calculations. Input tab - This tab displays a summary of the mapped Input stream as PHREEQC species.

OLIResults tab - This tab displays the key results of the calculations. Input tab - This tab displays a summary of the mapped Input stream as OLI species. Output

flows. This potentially enables recovery of some of the energy in the low grade steam. One of the methods of the Thermocompressor model in SysCAD is based

information required for Mass and Energy balance. See Model Examples for enthalpy calculation Examples. Unit Type: HotFlashTie - The first tab page in the access

displays the key results of the calculations. Input tab - Optional tab, only visible if Rxns.Option = TCE. This tab displays a summary of the mapped Input stream

information required for Mass and Energy balance. See Model Examples for enthalpy calculation Examples. Unit Type: CFMultiTie - The first tab page in the access

PHREEQCResults tab - This tab displays the key results of the calculations. Input tab - This tab displays a summary of the mapped Input stream as PHREEQC species.

SysCAD in the Examples folder, demonstrates the use of this model. The diagram shows the default drawing of the Counter Current Washer, with all of the streams

ChemAppResults tab - This tab displays the key results of the calculations. Input tab - This tab displays a summary of the mapped Input stream as ChemApp species.

AQSolResults tab - This tab displays the key results of the calculations. Input tab - This tab displays a summary of the mapped Input stream as AQSol species. Output

AQSolResults tab - This tab displays the key results of the calculations. Input tab - This tab displays a summary of the mapped Input stream as AQSol species. Output

Results. This tab displays the key results of the calculations. Input tab - This tab displays a summary of the Input stream. Output tab - This tab displays

PHREEQCResults tab - This tab displays the key results of the calculations. Input tab - This tab displays a summary of the mapped Input stream as PHREEQC species.

AQSolResults tab - This tab displays the key results of the calculations. Input tab - This tab displays a summary of the Input stream. Output tab - This tab displays

allows for inclusion of adsorption calculations in addition to precipitation. The PHREEQC Model Configuration allows for specification of precipitates which

information required for Mass and Energy balance. See Model Examples for enthalpy calculation Examples. Unit Type: Thickener1 - The first tab page in the access

Concentration, etc. The amount of any of the species may be zero. The Potash Properties Utility carries out all of the calculations using SI units and the calls

with SysCAD in the Examples folder, demonstrates the use of this model. The diagram shows the default drawing of the Washer, with all of the streams that

OLIResults tab - This tab displays the key results of the calculations. Input tab - This tab displays a summary of the mapped Input stream as OLI species. Output

exchangers as part of the model. (This is often more efficient when carrying out the modelling calculations.) The user sets the amount of flow to the heat

facility of up to two cake washes. See Example for the illustration of material splits with the various connections. The following shows the sequence of events

OLIResults tab - This tab displays the key results of the calculations. Input tab - This tab displays a summary of the mapped Input stream as OLI species. Output

AQSolResults tab - This tab displays the key results of the calculations. Input tab - This tab displays a summary of the mapped Input stream as AQSol species. Output

All of these equations rely on both the value of N and the relationship between N and the fraction of liquor remaining in the cake. An example of this

information required for Mass and Energy balance. See Model Examples for enthalpy calculation Examples. Additional fields are shown in Dynamic mode. These are

information required for Mass and Energy balance. See Model Examples for enthalpy calculation Examples. Unit Type: Tie-1 - The first tab page in the access window

OLIResults tab - This tab displays the key results of the calculations. Input tab - This tab displays a summary of the mapped Input stream as OLI species. Output

material is mixed in. This speed of this effect will depend on the relative flow entering the bed/CL versus the volume of the bed/CL zones. The following

CHEMAPPResults tab - This tab displays the key results of the calculations. Input tab - This tab displays a summary of the Input stream. Output tab - This tab displays

information required for Mass and Energy balance. See Model Examples for enthalpy calculation Examples. Unit Type: UnderflowWasher - The first tab page in the

purpose of the heap leach unit is to dynamically simulate the behaviour of a layered bed of ore being leached using solution added to the top of the heap

with solids - this is where you will set the size of the solids entering the plant; On the first tab of the Feeder, you will should see a heading called

the default drawing of the Hydrocyclone, with all of the streams that are available for operation of the unit. The physical location of the streams connecting

different folders. SysCAD 9.2 examples have been upgraded and improved to make use of new features. There are a number of new example projects. For detailed instructions

Sp tab, species calculations are not shown when the Filter is On except when the Calculations Only filter option is selected. Calculations are not included

information required for Mass and Energy balance. See Model Examples for enthalpy calculation Examples. Unit Type: TailingsDam - The first tab page in the access

discard any material. Here are some legitimate examples of this flexibility: Example 1: Target is Product Flow of 1 t/h solids so Product.Selection = Phase

fraction of component i in the Feed Ki Vapour-Liquid equilibrium Ratio of component i HF Enthalpy of Feed HV Enthalpy of Vapour fraction HL Enthalpy of Liquid

additional tab, R1. Depending on the number of reactions specified within the reaction file, there may be more than one of these tabs. The additional sections

User Calc (User Property Calculation) is defined as part of the project configuration file, please see User property Calculations for more information. This

50 g/L of NaCl(aq). We can set these values on the "DSp" tab: 1 kg/h of water, 20 g/h of KCl(aq) and 50 g/h of NaCl(aq). After we have entered these values

initialisation. Some examples are page activations, controllers on/off and variables which are referenced in the calculations/logic which is part of the Initialise_Prestart()

Model ➔ Species This tab page on the Plant Model Access Window has a number of parameters that the user may either set or read for Global settings.

information required for Mass and Energy balance. See Model Examples for enthalpy calculation Examples. The data sections and variable names are described in

be instead of the words Create New Configuration at the top of the window, you will see Create Copy of xxxxx, where xxxx is the file path of the configuration

93.db3 and try again. The use of TCE calculations at discrete locations within an overall flowsheet introduces the use of different enthalpy models at different

user-specified calculations must exist to allow mapping of the aqueous and organic values. Please see example 2 on how to set up user calculations. The model

Add-On and/or with Heat Calculations switched off. Topics covered in this section are: Heat of Formation Heat of Dilution Heat of Transition Please see Entropy

required flow. 2. Set Equipment Parameters in a number of Units at Start of a Run The user has a number of units that have the same settings, e.g. thickener

results of the FEM calculations. VCS Data tab - This tab displays a matrix of the species in the FEM reactions. The user may also enable the display of the

saying that Gangue consists of 1 atom of Gn which has a molecular weight of 100. (Normally this is the elemental composition of the species, such as Na2S1O4

Stream Heat of Formation values (Hf) for an example of how these individual heats of formation are used to determine the heat of formation of a stream. Notes:

Potash Solubility, Entering Solubility Data in the Species Properties Database The Solubility of a liquid or solid in a Solvent is the mass of that species dissolved

some calculations require specific aqueous species (mostly ionic species) to be defined within the project. The required species for each calculation are

number of independent PID controllers on the plant. The user may enter the required number of PID controllers in the Count field on the first page of the

a pipe where it is not required; To prevent the Demand from one of the outlet paths of a tank or tie from perpetuating downstream to where it is not required;

heat of reactions produced by those reactions. Note: For more information and examples on the mass and energy balance, please see Model Examples for example

Shows the use of Simple Heat Exchanger. Shows the use of Demand logic. Shows the use of Composition Fetch in a Feeder. Shows the use of Annotation Table

normally a derived value. However, the user may set the initial value of SAM or D entering the first precipitator to obtain the correct SAL, thus a correct

subroutines of the same name. Each function/subroutine contains user defined commands which are executed by SysCAD at different stages of the evaluation of the

Build 138 or earlier, please refer to Heat Calculations in the Calculation Selection. The Allow Heat Calculations option determines whether an energy balance

nullspace of [math]\displaystyle{ S }[/math]. The number of vectors ([math]\displaystyle{ J }[/math]) represents the degrees of freedom (or nullity) of the system

step 1 of edit configuration file, in Step 2 of edit configuration file - TCEs tab, select the location of the ChemApp_DAT_File folder (point 2 of workflow)

or more, of the solid species will behave differently in a unit operation to the other solid species. The Examples below demonstrate one of the Separation

Source) The Source can contain any number of species. Note the Source species may or may not also be added as part of the feed. Reactions using the Source species

do any calculations and has no process links to any other models in SysCAD flowsheets. Its sole purpose is for management and configuration of a selected

reactions. Entering Heat of Dilution Data in the Species Properties Database - Heat of dilution data is usually entered as a table of Enthalpy of Formation

user and is the species index of steam. Example: SteamIndex = SpI("H2O(g)") Please see Species Database Class for more examples. NOTE: These are old PGM Syntax

with SysCAD in the Examples Folder, demonstrate the use of this model in a SysCAD project. The diagram shows the default drawing of the Precipitator, with

diameter of a size interval. However there are other ways of characterizing the 'typical' diameter of a particle in a size interval (bin). For example, if the

Analysis 138. This file is stored in ..\SysCADXXX\Examples\01 Reports\Sensitivity Analysis.xlsm This is an example Excel Report using COM Automation for sensitivity

➔ Common Sections ➔ Define Species (DSp) Section This Tab will contain a list of all of the species that are specified in the Project configuration file. If a

Subcooling@P Calc The amount of Subcooling at the mixture's pressure (SatT@P-T). LatHtVap Calc The Latent heat of vaporisation of the listed component at the

information required for Mass and Energy balance. See Model Examples for enthalpy calculation Examples. Unit Type: Crusher2 - The first tab page in the access

information required for Mass and Energy balance. See Model Examples for enthalpy calculation Examples. Unit Type: SimpleHX - The first tab page in the access

results of these calculations are presented in Table 3. (Note that since the reference temperature of 273.15K is less than Ts (Start Temperature) of 298.15K

distributed with SysCAD in the Examples folder, demonstrates the use of this model. The diagram shows the default drawing of the Simple Heater, with the required

information required for Mass and Energy balance. See Model Examples for enthalpy calculation Examples. Unit Type: Pipe-1 - The first tab page in the access

In Step 2 of 2, select the Calculations tab Follow instructions given in Calculation Configuration The species display order (on Sp Tab of a stream) can

mix. If Heat of Dilution data is being used, it will usually be in the form of Spline data with Enthalpy of Formation at 25°C as a function of percentage

segments of the Layered Tank. (Each segment may consist of a number of Layers). Detail - This series of tabs allows the user to view the content of an individual

information required for Mass and Energy balance. See Model Examples for enthalpy calculation Examples. Unit Type: SimpleEvaporator - The first tab page in the

information required for Mass and Energy balance. See Model Examples for enthalpy calculation Examples. Unit Type: SimpleCondenser - The first tab page in the

documentation is for the latest version of SysCAD. The AQSol program can be used for general phase equilibrium calculations and process simulations for aqueous

growth rates of the order of 1[math]\displaystyle{ \mu/ }[/math]hr are typical. Knowing the actual surface area, we can then predict the rate of mass increase

To perform a mass balance of the species, we recommend using the TagSelect Class at the end of project solve, some examples are given below: ;--- SysCAD

videos in this section of the Help documentation are intended to supplement the Tutorial Document, and to provide clarification to some of the sections. Notes:

information such as Length of Run, Start Time, Step Size and so on at the start of the run. However, these tags can only be set while the project is stopped

selected, then other thermal calculations have no effect. Cooler calculations are still performed, so that the performance of the coolers is still available

Subcooling@P Calc The amount of Subcooling at the mixture's pressure (SatT@P-T). LatHtVap Calc The Latent heat of vaporisation of the listed component at the

elemental compositions of the SysCAD and ChemApp species must match. The charge of the two species must be the same. The redox state of each element is not

up and Viewing User Defined Calculations Another focus of this example is to show user how to add in user defined calculations for their project, once defined

fractions outside of the defined range the results may be invalid. This method calculates the viscosity of a solution based on ALL of the aqueous species

perform calculations. InFlow tab - This tab allows the user to set the final conditions, specify the InFlow composition and perform calculations. OutFlowS

account when calculating the properties of sugar solutions and in the calculation of purity and Brix. However, the split of the solutes for species other than

in Heat of Dilution in Reaction Energy Calculations and Partial Pressure of Gases in Reaction Energy Calculations. Summary of Reactions - Table of all reactions

Specify a Stream Flowrate (must have a flow to complete the calculations) Specify the Number of aqueous compounds to be defined (excluding water) Fill in

additional tab, R1. Depending on the number of reactions specified within the reaction file, there may be more than one of these tabs. The additional sections

user needs to define a Heat of Reaction (HOR) value for the reaction. See Heat of Reaction for more information. Entering Heat of Formation Data in the Species

AvePoints(number of points) - Reports the defined number of data points using time-weighted average. EndPoints(number of points) - Reports the defined number of data

displacement of feed liquor from the filter cake and will not be used in any of the wash efficiency calculations. The user may specify the wash efficiency of the

user needs to define a Heat of Reaction (HOR) value for the reaction. See Heat of Reaction for more information. Entering Specific Heat Data in the Species

balance calculations. Particle Growth increases the total mass of THA in the tank, without changing particle numbers. The growth calculations are completely

information required for Mass and Energy balance. See Model Examples for enthalpy calculation Examples. Unit Type: Pipe-1 - The first tab page in the access

temperature. These calculations will use a Reference Temperature of 25 °C. Note SysCAD uses a Reference Temperature of 0 °C for all enthalpy calculations, including

information required for Mass and Energy balance. See Model Examples for enthalpy calculation Examples. The data sections and variable names are described in

number of points such as the melting point of gallium and the triple point of hydrogen. The only water value it uses is the triple point of water of 273.16

ratios of vapours is reported. Custom Calculations: New functionality to specify calculations based on species in a stream. Two types of calculations based

range of the Cp value for any species. The image below shows the tab page for liquids in a project: Click on a property and you can choose from any of the

information required for Mass and Energy balance. See Model Examples for enthalpy calculation Examples. Unit Type: OLIReactor - The first tab page in the access

Model - Views Tab: Most of the calculations presented here have equivalent calculations in the Examples of User Property Calculations table. Please note that

Automation ➔ Example - Optimisation Related Links: Example Project - ChemApp with Python Optimisation This example demonstrates using a number of tools to

information required for Mass and Energy balance. See Model Examples for enthalpy calculation Examples. Unit Type: FFEvaporator2 - The first tab page in the

fixed feed (at start of belt) and the product to one fixed product (at end of belt). As the speed of the belt changes, the amount of material withdrawn from

side only. Examples include feeder inlets, sink outlets, spills, RB Source/Sink, etc. These DirectLinks do not have graphics symbols. The list of possible

next to the list. Most of the calculations presented here have equivalent calculations in the Examples of Species Calculations table. Please note that

Crystallisation Example and Three Stage Evaporator Example, which are distributed with SysCAD in the Examples Folder, demonstrate the use of the Potash species

information required for Mass and Energy balance. See Model Examples for enthalpy calculation Examples. Unit Type: DrumFilter - The first tab page in the access

name. The Histogram tab page provides a list of the values used to create the histogram. Note: If the value of the stattag is not a number (NAN) (shown as

form are as follows: Create a SysCAD report in Excel. User can use one of Example SysCAD Excel Reports or Default Reports as template. Once the Excel report

fraction of impurities retained or (4) entering constants for an equation which calculates the fraction of impurities retained. The dissolution of sugar crystals

size distribution of the screen feed, specifically the amount of near size material, the amount of half size material, and the amount of oversize material;

breakage. For example, if the feed contained 1 kg of +10mm material and 3 kg of +1.7mm material, then 95% of 1kg would be broken in the crusher. 30% of this broken

would have a number of tanks at different stages of the fill/precip/drain cycle, and the net operation is steady state; the contents of the product stream

default drawing of the Evaporative Dryer, with all of the streams that are required for operation of the unit. The physical location of the streams connecting

information required for Mass and Energy balance. See Model Examples for enthalpy calculation Examples. Unit Type: FFEvaporator1 - The first tab page in the

information required for Mass and Energy balance. See Model Examples for enthalpy calculation Examples. Unit Type: Compressor - The first tab page in the access

You need to take care of SysCAD requirements for data formatting and rules. NOTES: All engineering units are CASE sensitive. Most of the engineering unit

or more, of the solid species will behave differently in a unit operation to the other solid species. The Examples below demonstrate one of the Separation

information required for Mass and Energy balance. See Model Examples for enthalpy calculation Examples. Unit Type: SolidsRecovery - The first tab page in the

The main purpose of this unit operation is to simulate the transfer of heat through a body of material. Examples of this are linings of kilns or smelters

Shows the use of ChemApp Model Configuration. Shows the use of ChemApp Direct Calc Model Shows the use of ChemApp Side Calc Model Shows the use of ChemApp Reactor

with SysCAD in the Examples folder, demonstrate the use of this model in a SysCAD project. The diagram shows the default drawing of the Desuperheater,

use of PHREEQC Reactor. The use of PHREEQC Side Calc Model. The use of General Separator. The use of Makeup Sources and Makeup Blocks. The use of a General

SysCAD 9.3. See Revision History for a full list of improvements and fixes after the first release of Build 138. See Upgrading Projects and Upgrading Builds

breakage. For example, if the feed contained 1 kg of +10mm material and 3 kg of +1.7mm material, then 95% of 1kg would be broken in the mill. 30% of this broken

information required for Mass and Energy balance. See Model Examples for enthalpy calculation Examples. Unit Type: ReverseOsmosis - The first tab page in the

User Guide ➔ Edit ➔ Project Configuration (cfg File) ➔ Calculation Configuration ➔ Species Calculation Expressions NOTES: Function SumPhase() has only three

To use the negative of a declared variable in any function (where allowed), must enter -1 * variable (NOT -variable). For example y = exp(-x) is NOT allowed

information required for Mass and Energy balance. See Model Examples for enthalpy calculation Examples. Unit Type: MultiStorage - The first tab page in the access

The main purpose of this unit operation is to simulate the transfer of heat through a body of material. Examples of this are linings of kilns or smelters

window consists of 3 sections. This number may increase or decrease, based on user configuration. SignalCon tab - Contains a summary of all of the individual

information required for Mass and Energy balance. See Model Examples for enthalpy calculation Examples. Unit Type: DiskCentrifuge - The first tab page in the

information required for Mass and Energy balance. See Model Examples for enthalpy calculation Examples. Unit Type: Valve2 - The first tab page in the access

set-point of the PID controllers. When the project is converged, no additional acid is required via these Makeup blocks. This ensures stability of the project

the addition of reagents/utility to the plant. General Controller - This is used as a Feed Forward controller, as well performing calculations for control

L = water loading, mass flow of liquid per unit of ground area into the top of the tower (lb/h ft2) C = specific heat of water (assumed to be a constant

information required for Mass and Energy balance. See Model Examples for enthalpy calculation Examples. Unit Type: Classifier - The first tab page in the access

information of a selected variable, when copying the variable tag, please use "Copy Full Tag". For example: species or elemental flowrate of material flowing

specifies a reaction in a unit, the heat of reaction is calculated from the difference in the sum of the heats of formation of the products and reactants, as shown

Navigation: User Guide ➔ Edit ➔ Project Configuration (cfg File) ➔ Calculation Configuration ➔ User Property Expressions NOTES: Function SumPhase() has

SysCAD plant models of third-party software performing detailed equilibrium and thermodynamic property calculations. The direct integration of these specialist

Shows the use of precipitation using full particle size data. Brief Project Description As per Example 1. Full PSD is used instead of SSA. Project Configuration

Efficiency (MechEfficiency)}} }[/math] Checking of Steam conditions During the work calculations, checking of steam quality is important since the exhaust

Heats of formation of the products - Sum of Heats of formation of reactants. (This is the default method of calculating the heat of reaction.) The heats of

a film of molasses. The mass fraction of molasses is in the order of several percent of the total mass and the moisture fraction in the order of one percent

See Model Examples for enthalpy calculation Examples. Unit Type: Boiler - The first tab page in the access window will have this name. A) Example Project:

information required for Mass and Energy balance. See Model Examples for enthalpy calculation Examples. Unit Type: Pump2 - The first tab page in the access window

information required for Mass and Energy balance. See Model Examples for enthalpy calculation Examples. Unit Type: HeaterKX - The first tab page in the access

information required for Mass and Energy balance. See Model Examples for enthalpy calculation Examples. Unit Type: GasPump1 - The first tab page in the access

information required for Mass and Energy balance. See Model Examples for enthalpy calculation Examples. Unit Type: Pump-1 - The first tab page in the access

sections of the flowsheet where they are not needed. Various general improvements for entering Species Calculations and Properties Calculations New functions

specified to a fixed value of 2 t/h A simple heater unit model is used for the pre-heating stages of iron ore and hydrogen before entering the Shaft furnace. The

quick means of determining the effect of differing numbers of stages or wash water ratio in a CCD circuit. The user may also use a number of Counter Current

25 °C, the results of projects where the heat calculations are switched off may have some changes in results. The outlet temperature of all pipes is set

information required for Mass and Energy balance. See Model Examples for enthalpy calculation Examples. Unit Type:Valve-1 - The first tab page in the access

information required for Mass and Energy balance. See Model Examples for enthalpy calculation Examples. Unit Type: Valve-1 - The first tab page in the access

the same flash pressure. If different pressure drops are entered in the exit pipes (where number of FT > 1), then the higher pressure drop value will be used

Renamed Heats of Combustion. Tags will automatically update. Can no longer report on basis of normal volume flow. More checking of user calculation variable

information required for Mass and Energy balance. See Model Examples for enthalpy calculation Examples. Unit Type:Pump-1 - The first tab page in the access window

information required for Mass and Energy balance. See Model Examples for enthalpy calculation Examples. Unit Type: FFEvap3 - The first tab page in the access

Significantly enhanced the capabilities of calculations to allow simple and complex property and similar display of properties. Reorganised terms window,

volumetric flowrate of given stream P - pressure of given stream Subscripts: LPi - inlet conditions of Low Pressure stream HPi - inlet conditions of High Pressure

information required for Mass and Energy balance. See Model Examples for enthalpy calculation Examples. Unit Type: Reducer-1 - The first tab page in the access

information required for Mass and Energy balance. See Model Examples for enthalpy calculation Examples. Unit Type: Valve_NR-1 - The first tab page in the access

information required for Mass and Energy balance. See Model Examples for enthalpy calculation Examples. Unit Type: IonExchange - The first tab page in the access

information required for Mass and Energy balance. See Model Examples for enthalpy calculation Examples. Unit Type: FlashTank2 - The first tab page in the access

Case results worksheet Excel calculations returning statistic information for one of the resulting variables, in this example, the heating oil mass flow

Improved functionality of demand calculations in the network, as well as implementing new messages to provide feedback on Demand calculations that are not met

information required for Mass and Energy balance. See Model Examples for enthalpy calculation Examples. Unit Type: BasicPond - The first tab page in the access

VLEquilibrium sub model is capable of flash calculation. Here we are using the Flash Tank as an example. On the First Tab Page of the Flash Tank, select the Flash

➔ Density The Density of a substance, or mixture of substances, is defined as the ratio of the mass to the volume. Density is a function of temperature and pressure

information required for Mass and Energy balance. See Model Examples for enthalpy calculation Examples. Unit Type: Manifold - The first tab page in the access