CYPEFIRE FDS - Manual de utilizare CYPE
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Software for Architecture,
Engineering and Construction
CYPEFIRE
FDS
USER MANUAL
User manual of the CYPEFIRE FDS application for the design of
complex building models for the execution of fire evolution
simulations using the FDS fluid dynamics computational standard
("Fire Dynamics Simulator") developed by NIST ("National Institute of
Standards and Technology ", USA).
Contents
1
2
3
Basic Concepts......................................................... 3
1.1
Introduction ...................................................................... 3
1.2
Initial Setup and Starting a Project ................................ 3
1.3
CYPEFIRE FDS interface ................................................... 4
BIM Model ................................................................ 8
2.1
Libraries ............................................................................. 8
2.2
Model ............................................................................... 10
FDS Model ..
............................................................ 11
3.1
General data.................................................................... 11
3.2
Species ............................................................................. 17
3.3
Materials .......................................................................... 17
3.4
Surfaces ........................................................................... 23
3.5
Particles ........................................................................... 30
3.6
Reactions ......................................................................... 37
3.7
Device models................................................................. 41
3.8
Meshes ............................................................................. 49
3.9
Zones ................................................................................ 50
3.10 Obstructions.................................................................... 52
3.11 Hol
es ................................................................................ 55
3.12 Vents................................................................................. 56
3.13 Dispositive ....................................................................... 58
3.14 Controls ........................................................................... 72
3.15 Sections ............................................................................ 75
4
SLPXODWLRQ .......................................................... 77
4.1
Analysis/Calculation ....................................................... 77
4.2
Graphics ........................................................................... 78
1
Basic Concepts
1.1
Introduction
Thank you for choosing CYPE and CYPEFIRE FDS. CYPEFIRE FDS is a program created for
simulating the evolution of fires in complex building models using the computational
standard of fluid dynamics FDS (Fire Dynamics Simulator) developed by NI
ST (National
Institute of Standards and Technology, USA). This system is integrated in the Open BIM
workflow via the BIMserver.center using the IFC standard. CYPEFIRE FDS allows users to
import architectural data in the form of BIM models, define the elements of the model to
enable them to be fed into the simulation engine, and then simulate the design conditions
set by the user. The program carries out the necessary BIM model checks to ensure the
model is defined correctly.
Through the use of the SmokeViewer, the results of the analysis are able to be
visualized and with tools included for controlling the simulation. The SmokeViewer
includes tools for visualizing variables such as pressure, flow, temperature, etc. The
complexity involved in a dynamic simulation of fires in a building and the multiple factors
involved mean that the hardware and software requirements of the machine where this
simulation will be calculated are higher than what would be necessary to work normally
with oth
er CYPE programs.
1.2
Initial Setup and Starting a Project
This section of the manual will demonstrate how to start a project and begin using
CYPEFIRE FDS. Begin by downloading the latest version of CYPEFIRE FDS from the
BIMserver.center (https://bimserver.center/en/store/cypefire_fds), you will require a
BIMserver.center account, and an accessible IFC file model (Version 2019.e and above).
The first step is to open CYPEFIRE FDS. Next, connect to BIMserver.center on the far right
side and sign in if needed by following the prompted steps. Once signed in, a new project
can be created and an IFC file can be imported.
To continue working on a file, select File Manager under File and locate the desired
project. Otherwise, to start a new project, select New… under File, choose where the file
will be saved under Browse, and give the file a name and description if desired. After
continuing, a screen will appear regarding the BIMserver.center. Here is where a new
project within the BIMserv
er.center can be created by selecting “Create new project” or to
CYPEFIRE FDS / 3
connect the project with an existing project select Select project. From the list select the
appropriate project and click Accept.
The program will load the project selected and any files associated with the project. You
can then select which files you would like to import for the simulation. The BIM model will
automatically be imported as it is necessary for the simulation to function however; it is
also possible to import a CYPFIRE Sprinklers file to enable the simulation to include
sprinklers which are fully functional within the simulation. Clicking Accept will load the
configuration selected and open the main interface of the program with your model
loaded.
1.3
CYPEFIRE FDS interface
The CYPEFIRE FDS interface is comprised of two main areas separated by tabs at the top of
the window. The two tabs are: BIM Model, and FDS Model.
Fig. 1. FDS Interface
The BIM model tab is used to configure th
e necessary options to export the information of
the BIM model into the FDS model. The FDS model tab is used for configuring the
simulation itself. Both tabs are broken into 4 main sections: Primary toolbar (1), Selection
panel (2), Project tree (3), and the 3D Model window (4). Each section is highlighted in the
images below.
CYPEFIRE FDS / 4
Fig. 2. Interface sections
1.3.1
Primary toolbar
Fig. 3. Primary toolbars, “BIM Model” and “FDS Model” tabs
The primary toolbar contains the tools for controlling the configuration of the simulation.
In the BIM model tab, this consists of checking the model for errors and exporting the
model to the FDS model. The FDS model tab contains tools for altering the conditions of
the simulation, conducting the analysis, accessing the simulation, etc.
CYPEFIRE FDS / 5
1.3.2
Selection panel
Fig. 4. Selection panel
The selection panel is used to alter/input data for the corresponding element selected in
the Project tree. It is possible
to edit elements in the list, add new elements, delete
elements, or reorder elements using the blue arrows.
1.3.3
Project tree
In both tabs, BIM model
and FDS model, the
Project tree is broken
into two lists: Libraries
and Model. Each of
these will be explained
in further detail in the
appropriate
manual
sections below.
Fig. 5. Project trees (“BIM Model” left, “FDS Model” right)
CYPEFIRE FDS / 6
1.3.4
3D Model window
The 3D model window allows you to visualize the model in its current state. It is possible to
refresh the model to update any changes that have been made, to filter the layers, alter the
orientation, and to use slices to display the interior. For navigating the 3D view, the controls
are very similar to other CYPE programs. To pan the model, hold down the mouse wheel.
To rotate the model, hold the left or right mouse button down. To zoom, simply roll the
mouse wheel.
Fig. 6. 3D model
CYPEFIRE FDS / 7
2
BIM Model
2.1
Libraries
In this section of the tre
e we find the libraries where the main characteristics of the
elements imported from the BIM model are defined: Constructive elements, Gaps and
Sprinklers.
2.1.1
Construction elements
In the case of linking the project with a BIM model, the construction elements will be
shown in this part of the project tree.
When accessing it we can observe in the selection panel all the types of construction
elements that exist (facades, interior partitions, forged, defences, etc.). These must be
reviewed before exporting to the Model FDS tab. We can know that there are elements to
be defined since in the tree we will be indicated with an orange exclamation mark.
Fig. 7. Construction elements
CYPEFIRE FDS / 8
To define the constructive elements you
just have to enter the layers of which the
element is formed by defining:
- Layer reference (It will be used as the
description of the layer in the FDS Model
tab)
- Layer ID (It will be used to describe a
particular material of the layer in the
FDS M
odel tab)
- Thickness of the layer
Fig. 8. Construction element prompt
2.1.2
Openings
The openings are the elements that
represent both the doors and glazed
openings, and their definition is similar to
that of the building elements but the
breaking temperature must also be
defined for the element. Once this
temperature is reached in any of the
surfaces of the opening, it disappears from
the simulation.
Like the construction elements, an orange
exclamation marks the openings whose
layers have not been defined.
Fig. 9. Opening prompt
CYPEFIRE FDS / 9
2.1.3
Sprinklers
If there is sprinkler information in the BIM model (information that can be exported from
CYPEFIRE Sprinklers), all types of sprinklers present will appear here.
The only information in this section is the reference and the sprinkler ID, with the main
properties being defined in the FDS Model tab.
2.2
Model
2.2.1
Meshes
The meshes define the parts of the model in which the simulation is carried out, so all the
obj
ects involved in the calculation must be inside a mesh. In the simulation, more than one
mesh can be introduced.
Each mesh has its geometric position defined by 3 pairs of coordinates (x, y, z) and divided
into uniform cells. The size of the cells is recommended to have the same size in all three
directions. By default CYPEFIRE FDS will create a mesh containing the entire model with the
number of divisions needed in (x, y, z) to obtain a cell size of 0.20 x 0.20 x 0.20 m.
Fig. 10. Mesh prompt
CYPEFIRE FDS / 10
3
FDS Model
3.1
General data
3.1.1
Simulation time
CYPEFIRE FDS allows the configuration of the following parameters related to the
simulation time:
Fig. 11. Simulation time settings
•
Start time. Allows the indication of the moment in which the results of the simulation
will begin to be written into the output files of the FDS calculation engine
•
End time. Indicates the total duration of the simulation. If the value is 0, it only
generates the initial disposit
ion of the model, which allows a quick verification of the
geometry in the Smokeview window.
•
Initial time step. It is possible to indicate the initial time step of the simulation. By
default, this value is calculated automatically by dividing the size of a grid cell by the
characteristic flow rate. During the calculation, the time step is adjusted so that the
condition of CFL (Courant, Friedrichs, Lewy) is fulfilled. The FDS calculation engine uses
the following formula to obtain the value of the time step:
𝐷𝑇 =
1
5�𝛿𝑥 𝛿𝑦 𝛿𝑧 �3
�𝑔𝐻
CYPEFIRE FDS / 11
Where:
𝐷𝑇: Time steps [s]
𝛿𝑥 : Dimension in X of the smallest mesh cell
𝛿𝑦 : Dimension in Y of the smallest mesh cell
𝛿𝑧 : Dimension in Z of the smallest mesh cell
𝑔: Acceleration of gravity
𝐻: Height of the computational domain
•
Do not allow changes in the time step. Checking this option prevents the FDS
calculation engine from automatically adjusting the tim
e step.
•
Do not allow the time step to exceed the initial time step. By default, the time step
can never exceed the initial value. To allow this to happen it is possible to uncheck this
option.
3.1.2
Environment
CYPEFIRE FDS allows the configuration of the following parameters related to the ambient
environment in which the simulation is conducted:
Fig. 12. Environment settings
CYPEFIRE FDS / 12
•
Ground level - Indicates the value of the height above ground level in the simulation.
•
Humidity - Indicates the value of the relative humidity of the water vapour found in
the environment.
•
Atmospheric lapse rate - Indicates the variation of the ambient temperature
according to the height. A negative value indicates that the temperature drops with
height.
•
Maximum visibility - Indicates the maximum visibility value through smoke that can
be determined by the FDS calculation engine. The need to establish this value is due to
the inability, on the part of FDS, to r
eport an infinite value of visibility.
•
Noise - When activating this option, the FDS calculation engine initializes the flow field
with a very small amount of "noise" to avoid the development of a perfectly
symmetrical flow when the limit and the initial conditions are perfectly symmetrical.
•
Pressure - Indicates the ambient pressure at ground level.
•
Temperature - Indicates the temperature at the beginning of the simulation.
•
Visibility factor - Indicates the value of the constant used when calculating the
visibility across the smoke.
•
CO2 - Fraction of mass of carbon dioxide found in the environment.
•
O2 - Fraction of oxygen mass found in the environment.
•
Gravity - Indicates the three components of gravity. The value of the components of
gravity can be constant or as a function of time or position.
•
Wind speed - Indicates the wind speed in each direction at the beginning of the
simulation.
CYPEFIRE FDS / 13
3.1.3
Radiation
It is possible t
o configure the parameters used to carry out the calculation of the radiation
heat transmission equation. You can also disable the calculation of radiation, this saves
approximately 20% of CPU time.
Fig. 13. Radiation prompt
CYPEFIRE FDS permits the configuration of the following parameters related to the
calculation of radiation:
•
Use broadband model - When activated, the radiation calculator will use the
broadband model instead of the grey gas model used by default.
•
Number of angles
•
Angle increment - Indicates the increment over which the angles must be updated.
•
Time step increment - It indicates how often FDS must call the calculator of
transmission of heat by radiation.
•
Path length - It is used to determine the range of wavelengths over which the effective
absorption coefficients will be calculated. If not defined manually, FDS will default to a
step length value equal to five times the size of a mesh cell.
•
Radioactive source temperature - Indica
tes the value of the assumed temperature
for the radiation source. It is used in the spectral weighting, during the calculation of
the average cross sections of dispersion and absorption.
•
Number of angles in the integration of the Mie-phase function - Indicates the
number of angles used in the numerical integration of the Mie function. Increasing this
value will obtain a greater precision in the radioactive properties of the water particles.
CYPEFIRE FDS / 14
•
Absorption coefficient - By activating this option it is possible to establish a constant
absorption coefficient that will be used in simulations without combustion or species
that radiate.
Fig. 14. Radiation settings
3.1.4
Output parameters
CYPEFIRE FDS allows you to configure the following parameters related to the output files
of the simulation:
•
Number of data downloads in the output file, for each calculation.
•
Maximum number of Lagrangian particles. Indicates the maximum number of
Lagrangian particl
es that can be included simultaneously in a mesh.
•
Delete diagnosis. Activating this option will reduce the level of detail of information
about the status of the simulation shown in the output file with extension ".out".
•
Generate mass file of gaseous species. When activating this option, an output list will
be created with the total mass of all the species as a function of time. It must be borne
in mind that performing this calculation will considerably increase the time necessary
to perform the simulation.
•
Generate smoke and fire animation. Activating this option will produce an animation of
the smoke and fire that will be displayed during the simulation display in Smokeview.
CYPEFIRE FDS / 15
•
Speed error file. When activating this option, a file will be created with the maximum
error associated to the normal component of the speed in the solid or interpolated
limits.
•
Error file. Activating this option will generate an output file with extension ".notre
ady"
that will be deleted if the simulation is completed successfully.
•
Periodically delete the temporary output files. When activating this option, FDS will
periodically clean the temporary output files and write the data in the respective result
files. In this way you can easily visualize the model in Smokeview while the simulation
is being performed.
•
Precision of the output file. Indicates the number of significant digits of the mantissa
and the exponent in the numerical data entered in FDS.
•
Intervals of data writing in the output file.
•
Limit the maximum number of columns. When activating this option, the maximum
number of columns of the files with extension .csv will be limited where the data of the
devices (DEVC) and controllers (CTRL) are displayed.
Fig. 15. Output parameters
CYPEFIRE FDS / 16
3.2
Species
Gaseous species can be used as reactive species of the combustion model or as nonreactive species in the simulation of air flow.
It is possible to in
dicate the initial concentration of a predefined species in the simulation
through the initial mass fraction value of the gas, in the species section of the FDS model.
The FDS calculation engine creates by default an Air species that is defined as a compound
of N2, O2, CO2 and H2O. This species fills the space of the initial simulation environment that
has not been occupied by the rest of the species.
Species can be introduced into the simulation through the emission parameters of the
surfaces.
Fig. 16. Species selection window
3.3
Materials
The solid objects that make up the geometric model are often made up of several layers of
different materials. Therefore, to carry out the simulation, the thermal properties of each
of these materials must be specified. In the same way, it is also possible to specify the
characteristics of the liquid materials found in the scenario, which are used to represent
types of fuel.
CYPEFIRE FDS / 17
3.3.1
Properties
Within the Properties tab of the
Materials panel, it is possible to specify the following
parameters related to the thermal characteristics of the material:
•
Conductivity. It can be defined as a function of temperature by means of a ramp
function.
•
Density.
•
Specific heat. It can be defined as a function of temperature by means of a ramp
function.
•
Emissivity. Indicates the fraction of thermal radiation emitted by the material. Its value
must be between 0 and 1.
•
Absorption coefficient. Indicates the depth over which the material can absorb
thermal radiation.
Fig. 17. Material, properties
CYPEFIRE FDS / 18
3.3.2
Pyrolysis
The pyrolysis model of the material describes the reactions that occur during its
combustion process and the products that are generated.
The pyrolysis properties concerning solid and liquid materials are different. Consequently,
the type of material must be defined before specifying its characteristics.
Solid materials
3.3.2.1
Solid materials can have several associa
ted chemical reactions without the need for them
to occur at the same temperature.
The Pyrolysis tab of CYPEFIRE FDS allows you to configure the following general material
options:
•
Allow contraction of the material. When activating this option, to conserve the mass,
the thickness of the material will be reduced after a reaction process in which the
products have a higher density than the original material.
•
Allow the expansion of the material. When activating this option, to conserve the
mass, the thickness of the material will increase after a reaction process in which the
products have a lower density than the original material.
By adding a reaction to the material you must specify its kinetic properties and its
products.
The equation that FDS uses to determine the speed of the reaction is the following:
𝑛
𝑟𝑖𝑗 = 𝐴𝑖𝑗 𝑌𝑠,𝑖𝑠,𝑖𝑗 𝑒𝑥𝑝 �−
𝐸𝑖𝑗
𝑛
� 𝑋 𝑂2,𝑖𝑗 ;
𝑅𝑇𝑠 𝑂2
𝑌𝑠,𝑖 = �
Wher
e:
𝑟𝑖𝑗 : Speed of reaction to temperature 𝑇𝑠
𝜌𝑠,𝑖 : Material density [kg/m3]
𝜌𝑠 (0): Initial density of the layer [kg/m3]
𝑛𝑠,𝑖𝑗 : Order of reaction
𝐴𝑖𝑗 : Pre-exponential factor [s-1]
𝐸𝑖𝑗 : Activation energy [kJ/kmol]
𝑋𝑂2 : Local fraction of oxygen volume
𝑅: Universal constant of ideal gases (8,3143 J*K-1*mol-1)
CYPEFIRE FDS / 19
𝜌𝑠,𝑖
�
𝜌𝑠 (0)
The user can choose between manually entering the values of the pre-exponential factor
and the activation energy or calculating them from the following equation:
𝐸𝑖,𝑗 =
2
𝑒𝑟𝑝,𝑖 𝑅𝑇𝑝,𝑖
𝑌𝑠,𝑖 (0) 𝑇̇
Where:
𝑇𝑝,𝑖 : Reference temperature [⁰C]
𝑟𝑝,𝑖 /𝑌𝑠,𝑖 (0): Reference velocity [s-1]
𝑇̇: Heat rate [⁰C/min]
;
𝐴𝑖,𝑗 =
𝑒𝑟𝑝,𝑖 𝐸/𝑅𝑇
𝑝,𝑖
𝑒
𝑌𝑠,𝑖 (0)
In both cases the value of the reaction order must be specified, 𝑛𝑠 .
In cases where the
value of the reference temperature is not available, it can be
approximated from the pyrolysis range:
Where:
∆𝑇: Pyrolysis range [⁰C]
𝜐𝑠,𝑖 : Production of solid waste
𝑟𝑝,𝑖
2𝑇̇
=
(1 − 𝜐𝑠,𝑖 )
𝑌𝑠,𝑖 (0) ∆𝑇
To end up with the kinetic parameters, the program modifies the equation to define
pyrolysis models that do not follow the Arrhenius function.
𝑛
𝑟𝑖𝑗 = 𝐴𝑖𝑗 𝑌𝑠,𝑖𝑠,𝑖𝑗 𝑒𝑥𝑝 �−
Where:
𝑇𝑡ℎ𝑟,𝑖𝑗 : Threshold temperature [⁰C]
𝐸𝑖𝑗
𝒏
� 𝐦𝐚𝐱�𝟎, 𝑺𝒕𝒉𝒓,𝒊𝒋 �𝑻𝒔 − 𝑻𝒕𝒉𝒓,𝒊𝒋 �� 𝒕,𝒊𝒋
𝑅𝑇𝑠
In this case it will be necessary to enter the values of the threshold temperature, 𝑇𝑡ℎ𝑟 , and
the exponent of the reaction, 𝑛𝑡 .
Once the kinetic parameters that govern the reaction have been defined, the products
generated after the combustion and their quantity can be specified in th
e Products tab.
These can be both chemical species and other materials previously defined in the project.
Finally, it is possible to specify the heat values of the reaction, which indicates the amount
of energy per unit mass of the reactant that is consumed in the reaction, and the heat of
combustion that represents the amount of energy emitted per unit mass of the material
when subjected to a complete combustion in the presence of oxygen.
CYPEFIRE FDS / 20
It must be taken into account that the FDS calculation engine allows each solid material to
have a maximum of 10 associated reactions.
Fig. 18. Material, pyrolysis
Fig. 19. Reaction, kinetic parameters and products
CYPEFIRE FDS / 21
Liquid materials
3.3.2.2
Unlike solid materials, liquid fuels can only have an associated reaction.
It is possible to specify the following general properties:
•
Heat of combustion. It is the
amount of energy emitted per unit
mass of the material when
subjected
to
a
complete
combustion in th
e presence of
oxygen.
•
Boiling temperature. Temperature
at which the vapour pressure of the
liquid equals the vapour pressure
of the medium in which it is
located.
•
Latent heat of vaporization.
Energy required by the material to
change from liquid to gaseous
phase.
•
Allow
contraction
of
the
material. When activating this
option, to conserve the mass, the
thickness of the material will be
reduced after a reaction process in
Fig. 20. Liquid material, pyrolysis
which the products have a higher
density than the original material.
•
Allow the expansion of the material. When activating this option, to conserve the
mass, the thickness of the material will increase after a reaction process in which the
products have a lower density than the original material.
In terms of the products generated by the reaction, they can be both species and other
materials, in the same way as in the reactions of solid materials.
CYPEFIRE FDS / 22
3.4
Surfaces
The surfaces are used with t
he purpose of being able to specify the boundary conditions of
the different solid elements or openings located inside the computational domain.
The surfaces in CYPEFIRE FDS must have a unique reference and a colour. It is also possible
to indicate if it is adiabatic or, if not, to specify all the properties that define its behaviour.
To speed up this task, the Surface panel is structured based on the following tabs:
3.4.1
•
General properties
•
Thermal properties
•
Pyrolysis
•
Issue
•
Additional fields
Default surfaces
There are certain predefined surfaces within the FDS calculation engine, which have
particular characteristics. Consequently, when starting a new project in CYPEFIRE FDS these
surfaces will already be specified and it will not be possible to eliminate them.
•
INERT. Represents an inert wall at room temperature and is the default boundary
condition for all solid surfaces.
•
OPEN. It is only used to indicate that there is an opening to the out
side in the limits of
a mesh.
•
MIRROR. Represents a plane of symmetry. It is a surface without its own flow, which
allows a free movement and inverts the flow.
•
PERIODIC. This type of surface is used to establish periodic limits.
The surfaces of type OPEN, MIRROR and PERIODIC can only be assigned to entities of type
VENT (Vents) and these can only be located in the outer limits of a mesh.
CYPEFIRE FDS / 23
3.4.2
General properties
Within this group of parameters are the characteristics that define the general behaviour of
the surface.
First, it is possible to indicate the geometry of the surface. The solid objects introduced in
FDS are adjusted to the rectilinear geometry of the mesh; consequently, all physical entities
are represented as "boxes". The geometry of the surface can be used to describe the
thermal characteristics of spherical or cylindrical objects in the obstructions where it is
applied. In addition, in case of using the surface as a particle, the different
dimensions of
the geometry should be defined according to its type. The geometry classes available in
CYPEFIRE FDS are:
•
Cartesian.
•
Spherical.
•
Cylindrical.
CYPEFIRE FDS also allows the calculation engine to indicate that a surface is used as an
escape path between two pressure zones. When activating this option, you must indicate
the two pressure zones, previously defined, to which reference is made.
The surfaces that make up the solid objects can be formed by several layers and these, in
turn, can be composed of several materials. When adding a new layer to the surface, in
addition to listing the materials that make it up, you must establish a value for its thickness
and temperature.
Once the layers have been defined, CYPEFIRE FDS includes the option ‘Separation of layers’
which allows specifying the number of layers involved in the ejection of fuel vapour to the
outside of the surface. By default, the layer separation is 0.5 times the number of layers for
surfac
es with exposed back, and equal to the number of layers for the rest.
CYPEFIRE FDS / 24
Fig. 21. Surface, general properties
3.4.3
Thermal properties
The model of convection heat transmission that FDS uses in the simulation can be modified
in several ways. Below are the options that CYPEFIRE FDS allows us to use:
•
Default convection heat transfer model
o
In the LES calculation, the heat transfer coefficient h, measured in W/(m2 * K), is
determined from the following equation:
1 𝑘
ℎ = 𝑚𝑎𝑥 �𝐶�𝑇𝑔 − 𝑇𝑤 �3 , 𝑁𝑢�
𝐿
Where C is an empirical coefficient for natural convection, L is a characteristic
length related to the size of the physical obstruction, k is the thermal conductivity
of the gas and Nu is the Nusselt number.
CYPEFIRE FDS / 25
•
Logarithmic law of the wall
o
The local coefficient of heat transfer will be obtained from the following equation:
ℎ=
•
Specify the heat transfer coefficient
o
•
𝑛
𝜌𝑤 ∗
𝑐𝑝 ∗ 𝑢𝜏
𝑞̇ 𝑤
=
𝑇𝑔 − 𝑇𝑤
𝑇+
A constant value of the convection heat transfer coefficient can be directly
indicated.
Specify the heat flow on the solid surface
o
Instead of altering the heat transfer coefficient by convection, a fixed heat flow can
be specified directly. There are two ways to do it:
- Indicate the value of the net heat flow. FDS will calculate the surface temperature
necessary to ensure that the combined heat flux by radiation and convection is
equal to the net heat flux.
- Indicate the flow of heat by convection and the heat flow by radiation separately.
The heat flux by radiation will be determined from the emissivity and the
temperature of the surface.
The reverse side of a surface represents the boundary condition "behind" it. CYPEFIRE FDS
allows the selection of the following types of reverse:
•
Empty. It is assumed that the back of the wall is in an air space. The temperature of
this zone can be defined by the temperature
option on the back.
•
Exposed. It will allow the surface to transmit heat to the space behind the wall. This
option will only work if the wall is less than or equal to the thickness of a grid cell and if
there is volume of the computational domain on the other side of the wall.
•
Isolated. It is assumed that the wall is behind an insulating material, in which case
there will be no loss of heat to the material on the back.
In addition to the type of reverse, it is also possible to indicate a value for its emissivity.
The last group of options on this tab is related to the temperature. It is possible to indicate
the temperature of the outer limit of the surface which is used, together with the
emissivity, to determine the heat flux by radiation, when the total heat flow is specified in
CYPEFIRE FDS / 26
the radiation heat transmission options. The temperature of the surface may not be
constant and vary its value in time, to indicate that this occurs the ramp function option
is
included.
In the case that a reverse type of empty CYPEFIRE FDS has been selected, it is also possible
to set the temperature of the air space where the reverse side of the surface is located.
Fig. 22. Surface, thermal properties
3.4.4
Pyrolysis
Within this tab it is possible to detail the pyrolysis model that is carried out on the surface.
This can be defined by each of the parameters specified in the definition of the materials
that make up the surface or, on the contrary, you can establish specific properties. In both
cases, FDS can indicate if it is desired that the solid objects where the surface is used
disappear once they have been consumed. The objects will be eliminated from the
simulation cell by cell, as a consequence of the mass contained within each solid cell being
consumed by the pyrolysis reactions or by the defined heat emission rate.
CYPEFIRE FDS / 27
In the case of choosing the manual definition of the pyrolysis model, the following
parameters related to the
emission of heat and the ignition of the surface can be defined:
•
Emission of heat per unit area.
•
Speed of mass loss.
•
Ramp function. It allows describing non-constant behaviour, as a function of time, of
the heat emission from the surface.
•
Coefficient E. Empirical constant that depends on the properties of solid fuel material
and its geometrical configuration. It is used to calculate the reduction of the
combustion speed as a result of the presence of water.
•
Ignition temperature. Indicates the temperature from which the object will begin to
burn.
•
Vaporization heat. Indicates the amount of energy needed to burn the fuel.
When specifying the heat emission from the surface, you must choose between entering
the value of the heat emission per unit area or the speed of mass loss.
Fig. 23. Surface, pyrolysis
CYPEFIRE FDS / 28
3.4.5
Emission
By default, gaseous species do not penetrate solid surfaces. However, if it is desired to
indicate the existence
of a species emission flow, FDS provides two ways of doing so:
•
If the mass fraction of the species must have a known value within the flow, this value
can be indicated together with the flow velocity, the volumetric flow or the total mass
flow.
•
In case you want to represent the emission of species from your mass flow, you can
indicate this value and it will not be necessary to specify the flow velocity, the volumetric
flow or the total mass flow.
The options that CYPEFIRE FDS includes to define the characteristics of the flow are the
following:
•
Speed. The normal component of the speed is indicated by this parameter.
•
Volumetric flow. Instead of specifying the speed it is possible to indicate the
volumetric flow.
•
Total mass flow. Instead of specifying the speed it is possible to indicate the total
mass flow.
•
Ramp function. It allows describing non-constant behaviour, as a function of time,
flow velocity, volumetric flow or total mass flow.
•
Free sl
iding. This option allows you to adjust the surface tension to 0 (eliminates
viscous friction).
•
Wind profile. The speed of the wind profile at any outer limit will be constant by
default; however, FDS allows generating other profiles:
o
Parabolic. It produces a parabolic profile where the speed specified for the flow is
the maximum speed.
o
Atmospheric. Produces an atmospheric wind profile that follows the following
power law:
𝑢 = 𝑢0 (𝑧/𝑧0 )𝑃
For this case, the values of z0 and p must be specified. The parameter u0 corresponds to
the speed indicated for the flow while z is the height of the ground level specified in the
Environment options.
CYPEFIRE FDS / 29
A negative value of speed, volumetric flow or total mass flow will indicate that the flow is
directed into the computational domain while, if it is positive, the flow direction will point to
the outside of the domain.
Fig. 24. Surface, emission
3.5
Particles
Lagrangian particles can be used to represe
nt a wide variety of objects that are too small to
be solved in the numerical grid. The FDS calculation engine supports three classes of
Lagrangian particles: "Particles without mass", "Liquid particles" and everything else.
CYPEFIRE FDS / 30
3.5.1
3.5.2
Liquid particles
Description
•
Controller. FDS can control the presence of liquid particles in the simulation
depending on the response of a control or device.
•
Species. To define a liquid particle, you must specify the species that forms it. If a
liquid particle is assigned the species "WATER VAPOR" it will take the thermophysical
properties of the water, the radiative properties of the water and it will be coloured
blue in the Smokeview viewer.
•
Thermal properties. The "Heat of combustion" of the particle can be indicated. The
drops will evaporate in an amount equivalent to the fuel vapour in such a way that the
resulting heat release rate (assuming complete combustion) is equal to the
evaporation rate multiplied by
the "Heat of combustion".
•
Size distribution. The size distribution of the liquid particles is specified by a
cumulative volume fraction (FVC) indicated in the field "Type of distribution". The
default distribution is "Rossin-Rammler-Lognormal":
1. 𝐹(𝐷) =
⎧
⎪
𝐷 1
1
exp �−
∫
√2𝜋 0 𝜎𝐷′
�ln�
𝐷′
𝐷𝑉,0.5
2𝜎 2
⎨
𝛾
⎪1 − exp �−0.693 � 𝐷 � �
𝐷𝑉,0.5
⎩
2
��
� 𝑑𝐷′ (𝐷 ≤ 𝐷𝑉,0.5 )
(𝐷 > 𝐷𝑉,0.5 )
Where:
𝜎: Amplitude of the Lognormal distribution
𝛾: Amplitude of the Rosin-Rammler distribution
𝐷𝑉,0.5 : Mean diameter [μm]
Alternatively, it is possible to specify the distributions "Lognormal" or "Rosin-Rammler"
alone, instead of the combination of both. In order to avoid the FDS calculation engine
generating a size distribution, the type of distribution "Constant" can be indicated, in which
case all the particles will have a diameter equal to the "Mean diameter" in
dicated.
It is also possible to avoid generating infinitely large particles by specifying a "Maximum
diameter". Droplets smaller than the "Minimum Diameter" evaporates in a single step of
time.
CYPEFIRE FDS / 31
Fig. 25. Liquid particle, description
Visualisation
3.5.2.1
•
Colour. It is possible to indicate on the basis of which of the following properties we
want the particle to obtain its colour:
o Temperature
o Diameter
o Mass
o Duration
o Speed
If no property is specified, Smokeview will draw the particles in a single colour that can
also be indicated in this panel. By default, the water will be coloured blue and the rest
of the particles black.
CYPEFIRE FDS / 32
•
Number of particles. It is possible to define the "Sampling Factor" and the "Duration"
of the particles. The first parameter is used to reduce the size of the particle output file
that is used for the simulation in Smokeview. The default value for particles without
mass is 1 (all particles are seen in Smoke
view) and for the rest 10. On the other hand,
the "Duration" indicates the amount of time in which a particle exists in the simulation.
Fig. 26. Liquid particle, view
Radiative properties
3.5.2.2
The radiative properties of water and fuel are obtained automatically. In the case of fuel,
the properties of heptane are assumed.
•
Refractive indexes. It is possible to directly indicate the value of the "Real Refractive
Index" and the "Complex Refractive Index" in case these are considered constant.
Alternatively, values of these two parameters can be indicated as a function of the
wavelength.
CYPEFIRE FDS / 33
•
Orientation. In case the radiation heat flux is not evenly distributed around the
particle, it is possible to divide the particle into pieces, each with its own orientation.
Fig. 27. Liquid particle, radiative properties
3.5.2.3
Disintegration
It is possible to indicate that the particles may undergo secondary disintegration. In this
case, the "Surface tension" of t
he liquid and the "Breaking ratio" must be specified.
Optionally, you can indicate the indices of the distribution σ (Amplitude of the Lognormal
distribution) and Υ (Amplitude of the Rosin-Rammler distribution).
CYPEFIRE FDS / 34
Fig. 28. Liquid particle, breakup
3.5.3
Solid particles
The definition of the "Visualization", the "Radiative Properties" and the "Disintegration" of
the solid particles is the same as that corresponding to the liquid particles.
Description
3.5.3.1
•
Controller. FDS can control the presence of solid particles in the simulation depending
on the response of a control or device.
•
Surface. To define a solid particle, you must specify the surface that forms it and gives
it its properties.
CYPEFIRE FDS / 35
•
Movement. It is possible to indicate to the FDS calculation engine if a solid particle is
stationary.
•
Drag. Indicates the correlation of the drag coefficient as a function of the Reynolds
number based on the diameter of the particle
.
Fig. 29. Solid particle, description
CYPEFIRE FDS / 36
3.5.4
Particles without mass
Massless particles are the simplest Lagrangian particles and are used only for visualization.
Fig. 30. Massless particle, properties
3.6
Reactions
To define the combustion model that will be carried out during the simulation, the FDS
calculation engine allows the specification of the parameters that govern the behaviour of
the reaction.
Due to the cost of solving the transport equations, the FDS calculation engine only allows
an active reaction in the model. Consequently, it must be indicated in CYPEFIRE FDS which
reaction must be taken into account during the simulation using the Active option.
CYPEFIRE FDS / 37
3.6.1
Fuel
Within this tab CYPEFIRE FDS allows to select the method of definition of the type of fuel
that will be used in the reaction. The two options offered by the program are the following:
•
Simple chemical model. In the simple chemical model the form of the reaction is
a
lways assumed as:
𝐶𝑥 𝐻𝑦 𝑂𝑧 𝑁𝑣 + 𝜈𝑂2 𝑂2 → 𝜈𝐶𝑂2 𝐶𝑂2 + 𝜈𝐻2 𝑂 𝐻2 𝑂 + 𝜈𝐶𝑂 𝐶𝑂 + 𝜈𝑆 𝑆𝑜𝑜𝑡 + 𝜈𝑁2 𝑁2
Consequently, to define the chemical formula of the fuel, the number of carbon atoms
(C), hydrogen (H), oxygen (O) and nitrogen (N) must be specified.
•
By type of species. By defining the reaction in this way you can select a species that
acts as fuel, previously defined in the project.
Fig. 31. Reaction, fuel
CYPEFIRE FDS / 38
3.6.2
Products
CYPEFIRE FDS allows you to specify the amount of energy emitted by the combustion
reaction using the following parameters:
•
Heat combustion. It is used in the calculation of the enthalpy of fuel formation to
subsequently determine the emission of energy per unit volume of the chemical
reaction.
•
EPUMO2. Indicates the amount of energy emission per unit mass of oxygen
consumed. It is used to determine the Heat of combustion when its val
ue is not known.
•
Radiation fraction. This option allows the explicit specification of the fraction of the
total combustion energy that is emitted in the form of thermal radiation.
•
Ideal combustion heat. When activating this option, the Heat of combustion will be
reduced based on the values of Fraction of mass transformed into soot and Fraction of
mass transformed into CO. If EPUMO2 is defined instead of the Heat of combustion, its
value will not change.
The coefficients of the reaction products of the simple chemical model are computed
based on the following parameters:
•
Fraction of the mass transformed into soot. Indicates the fraction of fuel mass
transformed into smoke particles.
•
Fraction of the mass transformed into CO. Indicates the fraction of fuel mass
transformed into carbon monoxide.
•
Fraction of hydrogen atoms in soot.
From this data, the calculation engine FDS calculates the coefficients automatically in
the following way:
𝜈𝐶𝑂 𝜈𝐻2
𝑧
+
−
2
2
2
𝜈𝑂2 = 𝜈𝐶𝑂2 +
𝜈𝐶𝑂2 = 𝑥 − 𝜈𝐶𝑂 − (1 − 𝑋𝐻 )𝜈𝑆
𝜈𝐻2 𝑂 =
𝜈𝐶𝑂 =
𝑦 𝑋𝐻
−
𝜈
2 𝑆
2
𝜈𝑆 =
𝑊𝐹
𝑦
𝑊𝐶𝑂 𝐶𝑂
𝑊𝐹
𝑦
𝑊𝑆 𝑆
CYPEFIRE FDS / 39
𝜈𝑁2 =
𝑣
2
𝑊𝑆 = 𝑋𝐻 𝑊𝐻 + (1 − 𝑋𝐻 )𝑊𝐶
Where:
𝑦𝑆 : Mass fraction transformed into soot
𝑦𝐶𝑂 : Fraction of mass transformed into CO
X H: Fraction of hydrogen atoms in soot
Finally, it is possible to specify the values of the parameters that govern the suppression of
fire, these are:
•
Flame critical temperature. Indicates the temperature at which a diffusion flame
ceases to exist. In the combustion process, a diffusion flame is one in which the
oxidant is combined with the fuel by diffusion.
•
Auto ignition temperature. Indicates the minimum temperature for combustion to
occur.
Fig. 32. Reaction, products
CYPEFIRE FDS / 40
3.7
Device models
3
.7.1
Heat detector models
Heat detectors are devices capable of measuring temperature at a point using the
activation algorithm based on the Response Time Index, as a sprinkler but without
emission.
𝐶
𝑑𝑇𝑙 �|𝑢|
𝐶2
(𝑇𝑙 − 𝑇𝑚 ) −
=
𝛽|𝑢|
�𝑇𝑔 − 𝑇𝑙 � −
𝑅𝑇𝐼
𝑑𝑡
𝑅𝑇𝐼
𝑅𝑇𝐼
Where:
𝑢: Gas velocity
𝑅𝑇𝐼: Response time index
𝑇𝑙 : Sensor temperature
𝑇𝑔 : Gas temperature close to the sensor
𝑇𝑚 : Support temperature
𝛽: Fraction of volume of liquid water in the gas
𝐶: Experimentally determined factor that indicates the amount of heat conducted out of
the sensor by the support
𝐶2 : Constant determined empirically by DiMarzo (6 x 106 K/(m/s)1/2)
Fig. 33. Heat detector model
CYPEFIRE FDS / 41
3.7.2
Models of smoke detectors
Smoke detectors are devices capable of measuring the level of obscuration at a point. The
FDS calculation engine allows the introduction of Heskestad
and Cleary smoke detector
models.
•
Heskestad. The mass fraction of smoke in the detection chamber of the detector Yc is
located behind the mass fraction in the external free flow Ye in a period of time δt = L /
u, where u is the velocity of the free flow and L is the characteristic length of the
detector geometry. The change in the mass fraction of the smoke in the detection
chamber can be found by solving the following equation:
𝑑𝑌𝑐 𝑌𝑒 (𝑡) − 𝑌𝑐 (𝑡)
=
dt
L/u
The detector is activated when Yc exceeds the detector darkening threshold.
Fig. 34. Smoke detector
CYPEFIRE FDS / 42
•
Cleary. The Cleary model involves two filling times instead of one. The smoke must
first pass through the outer casing and then through a series of baffles before reaching
the detection chamber. There is a time lag associated with the passage of smoke
through the housing and also with the entry of smoke into the detection chamber. The
parameter δte indicates the character
istic filling time of the entire volume enclosed in
the external housing. The parameter δtc indicates the characteristic filling time of the
detection chamber. Cleary suggested that each characteristic fill time is a function of
the free flow velocity u outside the detector.
δt e = αe uβe ;
δt c = αc uβc
The parameters α and β are empirical constants related to the specific geometry of the
detector. The change in the mass fraction of smoke in the detection chamber Yc can be
determined by solving the following equation:
𝑑𝑌𝑐 𝑌𝑒 (𝑡 − δt e ) − 𝑌𝑐 (𝑡)
=
dt
δt c
Where Ye is the mass fraction of the smoke outside the detector in the free flow.
3.7.3
Thermocouple models
The output value of a thermocouple is the temperature of the device itself. The
temperature of the thermocouple differs from the gas by an amount relative to the size of
the sphere. This can be determined using the thermocouple temperature equation, TTC.
𝜌𝑇𝐶 𝑐𝑇𝐶
𝑑𝑇𝑇𝐶
4
= 𝜀𝑇𝐶 (𝑈/4 − 𝜎𝑇𝑇𝐶
) + ℎ(𝑇𝑔 − 𝑇𝑇𝐶 ) = 0
𝑑𝑡
Where:
𝜀𝑇𝐶 : Emissivity of the thermocouple
𝑈: Integrated radiative intensity
𝑇𝑔 : Actual gas temperature
ℎ: Coefficient of heat transmission to a small sphere, ℎ = 𝑘𝑁𝑢/𝐷𝑇𝐶
In the thermocouple model panel you must specify the diameter value, the emissivity, the
density and the specific heat of the sphere. It is possible to force the value of the heat
transfer coefficient in case you do not want to use the calculated value. The default
values for the density and specific heat of the sphere are those of nickel; 8908 kg / m3 and
0.44 kJ / kg / K.
CYPEFIRE FDS / 43
Fig. 35. Thermocouple model
3.7.4
Sprinkler models
Definition
3.7.4.1
•
Particle. Indicates the particle that is going to be sprayed by the device.
•
Activation. In the FDS calculation engine, sprinklers are activated according to the
standard RTI algorithm (Respon
se Time Index).
2.
𝑑𝑇𝑙
𝑑𝑡
=
�|𝑢|
�𝑇𝑔
𝑅𝑇𝐼
− 𝑇𝑙 � −
𝐶
(𝑇
𝑅𝑇𝐼 𝑙
𝐶
2
− 𝑇𝑚 ) − 𝑅𝑇𝐼
𝛽|𝑢|
Where:
𝑢: Gas velocity
𝑅𝑇𝐼: Response time index
𝑇𝑙 : Sensor temperature
𝑇𝑔 : Gas temperature close to the sensor
𝑇𝑚 : Sprinkler support temperature
𝛽: Fraction of volume of liquid water in the gas
𝐶: Experimentally determined factor that indicates the amount of heat conducted out
of the sensor by the support
𝐶2 : Constant determined empirically by DiMarzo (6 x 106 K/(m/s)1/2)
CYPEFIRE FDS / 44
Fig. 36. Sprinkler model, definition
Flow
3.7.4.2
•
Flow. The spray flow can be indicated by specifying the value of the "Volumetric flow"
or the "Mass flow rate". As an alternative, it is possible to indicate the value of the "KFactor" and the "Operating Pressure". In this last case the volumetric flow is calculated
from the following equation:
•
Where:
𝐾: Fac
tor K [L/(min*bar1/2)]
𝑝: Operating pressure [bar]
𝐾�𝑝
Initial position. The value of the radius (m) of a sphere around the sprinkler where the
water droplets are initially placed in the simulation is indicated. It is assumed that
beyond this sphere the drops have completely broken and move independently.
CYPEFIRE FDS / 45
•
Particles. The number of particles inserted every second is indicated by each active
sprinkler.
Fig. 37. Sprinkler model, flow
Sprinkler pattern
3.7.4.3
•
Simple pattern.
o Distribution. Indicates how the drops are distributed within the specified "Spray
Angle". The available options are "Gaussian" and "Uniform. In the case of selecting
the "Gaussian" distribution, you must specify the value of the "Latitude of the
maximum density of particles" and the "Width of the distribution".
o Speed of the particles. Indicates the speed of the drops at their insertion point.
o Spray angle. The pair of angles through which the particles are sprayed is
indicated.
The angles draw a conical pattern relative to the south pole of the sphere centered
on the sprinkler with a radius equal to that indicated for the "Initial position".
•
Complex pattern.
CYPEFIRE FDS / 46
• Table. For complex spray patterns, it is possible to use a table of values with the
spherical distribution for each solid angle. "Latitude 1" and "Latitude 2" are the
limits of the solid angle measured in degrees from the south pole (0 is the south
pole and 90 is the equator, 180 is the north pole). The parameters "Length 1" and
"Length 2" are the limits of the solid angle (also in degrees), where 0 (or 360) is
aligned with the x axis and 90 is aligned with the y axis. Finally, you must specify the
"Velocity" of the drops at their insertion point and the fraction of the total liquid flow
that must emerge from that particular solid angle ("Flow fraction").
Fig. 38. Sprinkler model, spray pattern
CYPEFIRE FDS / 47
3.7.5
Nozzle models
The nozzles are devices sim
ilar to sprinklers, the difference is that they are not activated
based on the standard model RTI (Response Time Index).
The definition of "Flow" and "Sprinkler pattern" is equivalent to that described in the
previous section corresponding to the "Sprinkler models".
Fig. 39. Nozzle model, flow
CYPEFIRE FDS / 48
Fig. 40. Nozzle model, spray pattern
3.8
Meshes
The meshes constitute the computational region of the simulation, which implies that all
the objects involved in the calculation must be inside a mesh. A mesh is a parallelepiped
defined by two points that correspond to two of its opposite corners.
In a simulation, more than one mesh can be introduced in order to execute the calculation
in parallel through MPI (Message Passing Interface).
Each mesh is subdivided into uniform cells. The size of the cells should be approximately
the same in all three directions to obtain an optimum degree of accuracy.
It should be noted that the FDS calculation engine uses the fast Fourier tran
sform (FFTs) to
determine the pressure in the y and z directions, and this algorithm is more efficient when
the number of cells in those directions can be factored into low cousins, such as 2, 3 and 5.
CYPEFIRE FDS / 49
The number of cells in the x direction is not affected because FFTs are not used in the x
direction.
Fig. 41. Mesh
3.9
Zones
Through the pressure zones it is possible to model closed regions of the computational
domain that have their own level of ambient pressure. The FDS calculation engine is not
able to identify these spaces based solely on the location of the obstructions, therefore, it
is necessary to indicate where they are located and what their dimensions are. To do this,
you must specify in CYPEFIRE FDS the values of the geometric coordinates that define the
edges of the rectangular area. In case the region is not rectangular, the FDS calculation
engine will extend the boundaries of the zone to make up the non-rectangular region.
To indicate that a pressu
re zone is linked to another, through ducts or other connections,
CYPEFIRE FDS allows to indicate the existence of a leakage area and the dimensions of it.
By default, the External zone is defined, which has the ambient pressure introduced in the
Environment options of the toolbar.
CYPEFIRE FDS / 50
Fig. 42. Zone
3.9.1
Initial regions
An FDS simulation begins with the environmental conditions defined in the "Environment"
options for the entire scene. This is usually valid for most cases; however, it is sometimes
convenient to modify the environmental conditions in a specific region of the
computational domain. The initial regions are rectangular spaces that allow this function to
be carried out.
•
Limits of the region. Indicates the coordinates of the two points that define the
position and dimensions of the initial region.
•
Properties. It is possible to indicate a value of "Density", "Temperature" and "Emission
of heat per unit volume" different from that defined in the "
Environment" options.
•
Species. Indicates the presence and concentration of species in the initial region.
CYPEFIRE FDS / 51
Fig. 43. Initial region
3.10
Obstructions
The obstructions are rectangular solids whose sides are parallel to the planes of the
coordinate axis. These are the main FDS entities used to generate the 3D geometric model
in order for it to be simulated.
The colour of the complete obstructions can be indicated, and in the case that they are not,
the colours on the surfaces of each face of the object will be used in the simulation instead.
3.10.1 Definition
General parameters can be defined in this tab such as the definition of the project’s
geometry and the activation of the obstruction.
CYPEFIRE FDS / 52
•
Controller. The window shows how the FDS controls the presence of an obstruction in
the simulation depending on the response of a control or device. This way, events can
be modelled such as the breakage of the windows due to the rise of the tempe
rature.
•
Limits of the object. This window indicates the coordinates of the two points that
define the position and dimensions of the obstruction.
•
Texture. This window indicates the origin of the texture used in the surfaces that
make up the obstruction.
Fig. 44. Obstruction, definition
3.10.2 Properties
In this tab, the main properties of the obstruction can be accessed and the visualization
and interpretation of its geometry can be generated by the FDS engine.
•
Allow gaps (HOLE). Activating this option will allow the obstruction to be penetrated
by hole-type objects (HOLE).
CYPEFIRE FDS / 53
•
Allow vents (VENT). Activating this option will allow the placement of vent-type objects
(VENT) on the surfaces of the obstruction.
•
Rejectable. Activating this option will allow the program to discard the obstruction of
the calculation.
•
Overlap. If the faces of two obstructions overlap, FDS will use the properties of the
obstruction that was defined second. If
this is not desired, activate this option in the
second obstruction so that FDS uses the properties of the first one.
•
With thickness. Activating this option will force the object to occupy the space of a cell
in the mesh. This prevents FDS from approaching thin obstructions to 2D surfaces.
•
Draw outline. When activating this option, the obstruction will no longer be
represented as a solid in the simulation and only its outline will be shown.
•
Apparent density. The apparent density is used to determine the mass of fuel of the
solid object. This parameter overwrites the rest of the variables from which the mass
of fuel would be calculated.
Fig. 45. Obstruction, properties
CYPEFIRE FDS / 54
3.10.3 Surfaces
In this tab, types of surfaces can be indicated and generate the 6 faces of the rectangular
block. Therefore, it is possible to specify a single type of surface for all the obstruction or
different surfaces for each plane. By default, obstructions in FDS are created
with the
predefined surface INERT.
Fig. 46. Obstruction, surfaces
3.11
Holes
Holes are blocks that are rectangular solids whose sides are parallel to the planes of the
coordinate axis, the same as the obstructions. These subtract their volume to the
obstructions that intersect, whenever it has been indicated previously that they are allowed
to contain holes.
By default, the holes are transparent elements in the FDS model; however, it is possible to
set it to a specific colour.
CYPEFIRE FDS / 55
3.11.1 Definition
Within this tab, the general parameters that define the geometry and activate the holes can
be located.
•
Controller. FDS controls the presence of a hole in the simulation depending on the
response of the control or device.
•
Limits of the object. Indicates the coordinates of the two points that define the
position and dimensions of the hole.
Fig. 47. Hole
3.12
Vents
The vents are flat and adjacent to the obstructions or the boundaries of the mesh. They
can be
used to model components of the building's ventilation system, such as a diffuser
or a return.
3.12.1 Definition
Within this tab, the general parameters that define the location and activation of the vent
can be located.
CYPEFIRE FDS / 56
•
Controller. FDS controls the presence of a vent in the simulation depending on the
response of a control or device.
•
Limits of the object. Indicates the coordinates of the two points that define the
position and dimensions of the vent.
•
Texture. Indicates the origin of the texture used on the surface used by the vent.
Fig. 48. Vent, definition
3.12.2 Properties
Within this group of parameters are the characteristics that define the general behaviour of
the vent.
•
Surface. It is possible to indicate a surface for the vent different from the obstruction
that accompanies it. The predefined surfaces OPEN, MIRROR and PERIODIC can be
applied to the vents to indicate a special behaviour.
CYPEFIRE FDS / 57
•
Geometry. The shape
of the vent can be chosen to be circular or semicircular, which
means that the radius must be indicated. The normal direction of the vent can also be
forced into one of the coordinate axes (positive or negative).
•
Radial propagation of fire. It is possible to indicate to the FDS that the fire will
propagate radially on the surface of the vent. To do this, the propagation speed and
the starting point must be specified.
Fig. 49. Vent, properties
3.13
Dispositive
The devices can be used to record the value of a specific parameter at a point in the
simulation or to represent the mathematical model of a complex sensor, such as smoke
detectors, sprinklers or thermocouples.
CYPEFIRE FDS / 58
3.13.1 Gas
3.13.1.1
phase measuring devices
Definition
Within this tab, the general parameters that define the location and activation of the
gaseous phase measurement device are specified.
•
Controller. FDS controls the presence of a gaseous phase measurement device in the
simulation dep
ending on the response of a control or device.
•
Type of measurement. Indicates whether the user wants to perform a "Spot"
measurement or obtain an "Integrated quantity" of a plane or volume of the space.
•
Position. Indicates the coordinates corresponding to the location of the gaseous phase
measurement device in the scene, as well as the components of its direction vector
and its rotation.
Fig. 50. Gas phase measuring device, definition
CYPEFIRE FDS / 59
3.13.1.2
Properties
Within this group of parameters are the characteristics that define the general behaviour of
the gaseous phase measurement device.
•
Quantity of measurement. Indicates the "Quantity" that the gaseous phase
measuring device must measure during the simulation. It can activate the option
"Statistical results" in order to obtain a statistical value of the quantity measured
(Maximum value, Minimum value, Average value ...).
•
Activation. Indicates a value as "Control point" that indicates when the
gas phase
measuring device changes state.
o Allow a single change of state. When activating this option, the gaseous phase
measurement device can only change state once in the simulation.
o Initially activated. When activating this option, it indicates that the gas phase
measurement device is activated at the beginning of the simulation.
Fig. 51. Gas phase measuring device, properties
CYPEFIRE FDS / 60
3.13.2 Solid
3.13.2.1
phase measurement devices
Definition
Within this tab, the general parameters that define the location and activation of the solid
phase measurement device are required.
•
Controller. FDS controls the presence of a solid phase measurement device in the
simulation depending on the response of a control or device.
•
Type of measurement. Indicates whether the user wants to perform a "Spot"
measurement or obtain an "Integrated quantity" of a plane or volume of the solid.
•
Position. Indicates the coordinates corresponding to the location of the solid p
hase
measurement device in the scene, as well as the "Normal direction to the surface of
the solid".
Fig. 52. Solid phase measuring device, definition
CYPEFIRE FDS / 61
3.13.2.2
Properties
Within this group of parameters are the characteristics that define the general behaviour of
the solid phase measurement device.
•
Quantity of measurement. Indicates the "Quantity" that the solid phase
measurement device must measure during the simulation. It is possible to activate the
option, "Statistical results", with the purpose of obtaining a statistical value of the
measured quantity (Surface integral).
•
Activation. Indicates a value as "Control point", which show users when the solid
phase measurement device changes state.
o Allow a single change of state. When activating this option, the solid phase
measurement device can only change status once in the simulation.
o Initially activated. When activating this option, the solid phase measurement
device is activated at the beginni
ng of the simulation.
Fig. 53. Solid phase measuring device, properties
CYPEFIRE FDS / 62
3.13.3 Heat
3.13.3.1
detectors
Definition
Within this tab, the general parameters that define the location and activation of the heat
detector are required.
•
Controller. FDS controls the presence of a heat detector in the simulation depending
on the response of a control or device.
•
Position. Indicates the coordinates corresponding to the location of the heat detector
in the scene, as well as the components of its direction vector and its rotation.
Fig. 54. Heat detector, definition
3.13.3.2
Properties
Within this group of parameters are the characteristics that define the general behaviour of
the heat detector.
•
Model of heat detector. Indicates the "Heat detector model", that was previously
defined, whose properties will be applied to the device.
CYPEFIRE FDS / 63
•
Activation.
o Allow a single change of state. Activating this option allows the heat detector to
only
change state once in the simulation.
o Initially activated. This option activates the heat detector at the beginning of the
simulation.
Fig. 55. Heat detector, properties
3.13.4 Beam detectors
3.13.4.1
Definition
Within this tab, the general parameters that define the location and activation of the beam
detector are required.
•
Controller. FDS controls the presence of a beam detector in the simulation depending
on the response of a control or device.
•
Beam position. Indicates the coordinates corresponding to the location of the beam
detector in the scene, as well as the components of its direction vector and its rotation.
CYPEFIRE FDS / 64
•
Activation. Showcases a value as "Control point" that indicates when the beam
detector changes state.
o Allow a single change of state. When activating this option, the beam detector can
only change state once in the simulation.
o Initially activated. Activating this option indicates that the beam detector is
activated at the beg
inning of the simulation.
Fig. 56. Beam detector
3.13.5 Smoke detectors
3.13.5.1
Definition
Within this tab, the general parameters that define the location and activation of the smoke
detector are required.
•
Controller. FDS controls the presence of a smoke detector in the simulation
depending on the response of a control or device.
•
Position. Indicates the coordinates corresponding to the location of the smoke
detector in the scene, as well as the components of its direction vector and its rotation.
CYPEFIRE FDS / 65
Fig. 57. Smoke detector, definition
3.13.5.2
Properties
Within this group of parameters
are the characteristics that define
the general behaviour of the
smoke detector.
•
Model of smoke detector.
Indicates that the "Smoke
detector
model",
as
previously
defined,
has
properties that will
applied to the device.
•
be
Activation.
Fig. 58. Smoke detector, properties
o Allow a single change of
state. When activating this
option, the smoke detector can
only change status once in the simulation.
o Initially activated. When activating this option, the smoke detector is activated at
the beginning of the simulation.
CYPEFIRE FDS / 66
3.13.6 Smoke layer
3.13.6.1
height meters
Definition
Within this tab, the general parameters that define the location and activation of the height
meter of the smoke layer are specified.
•
Controller. FDS controls the presence of a height meter of the smoke layer in the
simulation depending on the response of a control or device.
•
Position. Indicates the coordinates corresponding to the location of the height meter
of the smoke layer in the scene.
Fig. 59. Smoke layer height measurement device, definition
3.13.6.2
Properties
Within this group of parameters are the characteristics that define the general behaviour of
the height meter of the smoke layer.
•
Quantity of measurement. Indicates the quantity to be measured by the height
meter of the smoke layer (layer height, maximum temperatu
re or minimum
temperature).
CYPEFIRE FDS / 67
•
Activation. Showcases a
value as "Control point"
that indicates when the
height meter of the smoke
layer changes state.
o Allow a single change
of
state.
When
activating this option,
the height meter of the
smoke layer can only
change status once in
the simulation.
o Initially
activated.
When activating this
option,
the
height
meter of the smoke
layer is activated at the
beginning
of
the
simulation.
Fig. 60. Smoke layer height measurement device, properties
3.13.7 Thermocouples
3.13.7.1
Definition
Within this tab, the general
parameters that define the
location and activation of the
thermocouple are required.
•
Controller. FDS controls
the
presence
of
a
thermocouple
in
the
simulation depending on
the response of a control
or device.
•
Fig. 61. Thermocouple, definition
Position. Indicates the coordinates corresponding to the location of the thermocouple
in the scene, as well as the components of its direction vector and i
ts rotation.
CYPEFIRE FDS / 68
3.13.7.2
Properties
Within this group of parameters are the characteristics that define the general behaviour of
the thermocouple.
•
Thermocouple model. Indicates that the "Thermocouple model", which was
previously defined, has properties that will be applied to the device.
•
Activation. Showcases a value as a "Control point" which indicates when the
thermocouple changes state.
o Allow a single change of state. When activating this option, the thermocouple can
only change its status once in the simulation.
o Initially activated. When activating this option, the thermocouple is activated at
the beginning of the simulation.
Fig. 62. Thermocouple, properties
CYPEFIRE FDS / 69
3.13.8 Sprinklers
3.13.8.1
Definition
•
Controller. FDS controls the presence of a sprinkler in the simulation depending on
the response of a control or device.
•
Position. It indicates the coordinates corresponding to the location of the sprinkler in
the scene,
as well as the components of its direction vector and its rotation.
Fig. 63. Sprinkler, definition
3.13.8.2
Properties
•
Sprinkler model. Indicates that the "Sprinkler Model", which was previously defined,
has properties that will be applied to the device.
•
Activation. It is possible to limit the logical state of the device to a single change, so
that the sprinkler can be put into operation but not stopped or vice versa. In addition,
it can be indicated that the device is activated at the beginning of the simulation.
CYPEFIRE FDS / 70
Fig. 64. Sprinkler, properties
3.13.9 Nozzles
3.13.9.1
•
Definition
Controller. FDS controls the
presence of a nozzle in the
simulation depending on the
response of a control or
device.
•
Position. It indicates the
coordinates corresponding
to the location of the nozzle
in the scene, as well as the
components of its direction
vector and its rotation.
Fig. 65. Nozzle, definition
CYPEFIRE FDS / 71
3.13.9.2
Properties
•
Nozzl
e model. Indicates that
the "Mouthpiece Model",
which
was
previously
defined, has properties that
will be applied to the device.
•
Activation. Indicates when
the nozzle in the simulation
will be activated.
Fig. 66. Nozzle, properties
3.14
Controls
The controls are mechanisms that
allow the users to describe
behaviours
with
greater
complexity than with the devices.
•
Function. Indicates the type of
control function.
o ANY. The status of the
control changes if any of
the devices or controls
defined as "Input variables"
is activated.
o ALL. The status of the
control changes if all the
devices or controls defined
as "Input variables" is
activated.
Fig. 67. Control
CYPEFIRE FDS / 72
o ONLY. The status of the control changes if only N of the devices or controls defined
as "Input variables" are activated. The value of N is entered through the field
"Minimum number of variables".
o AT_LEAST. The control status changes if at least N of the devices or controls defined
as "Input vari
ables" are activated. The value of N is entered through the field
"Minimum number of variables".
o TIME_DELAY. The state of the control changes after a time interval ("Delay time")
since the device or control defined as "Input variable" is activated.
o CUSTOM. The status of the control changes based on the result of the ramp
function entered as "Input variable".
o DEADBAND. The state of the control changes based on the value of the device
defined as "Input variable" in a manner analogous to the operation of a thermostat.
If the value of the "Dimension" parameter is "Lower", the status of the control will
change when the value of the "Input variable" falls below the "Lower control point".
The opposite operation will occur when the value of "Dimension" is "Superior".
o KILL. The simulation will be interrupted when the device or control defined as
"Input variable" is activated.
o RESTART. A restart file will be generated when the device or control defined as
"Input variable" is activated.
This way, the simulation can be restarted later from this
point.
o SUM. The value of the control is the sum of the devices, controls and, optionally, the
constant defined as "Input variables".
o SUBSTRACT. The value of the control is the subtraction of the device, control or
constant defined as "Subtracting" the value of the device, control or constant
defined as "Minuend".
o MULTIPLY. The value of the control is the multiplication of the devices, controls and,
optionally, the constant defined as "Input variables".
o DIVIDE. The value of the control is the division of the device, control or constant
defined as "Divisor" to the value of the device, control or constant defined as
"Dividend".
o POWER. The value of the control is the result of the power with base equal to the
value of the device or control defined as "Base" and exponent equal to the value of
the device or control defined as "Exponent".
CYPEFIRE FDS / 73
o EXP. The value of the control is the exponential of the device o
r control defined as
"Input variable".
o LOG. The value of the control is the natural logarithm of the device or control
defined as "Input variable".
o COS. The value of the control is the cosine of the device or control defined as "Input
variable".
o SIN. The value of the control is the sine of the device or control defined as "Input
variable".
o ACOS. The value of the control is the arccosine of the device or control defined as
"Input variable".
o ASIN. The value of the control is the arcsine of the device or control defined as
"Input variable".
o PID. A PID control function (Proportional Integral Derivative) is a feedback controller
commonly used to control electrical and mechanical systems. The function
calculates an error between a process variable ("Input variable") and a desired set
point ("Control point"). The purpose of the PID function is to minimize the error. A
PID control function is calculated as:
𝑡
𝑢(𝑡) = 𝐾𝑝 𝑒(𝑡) + 𝐾𝑖 � 𝑒(𝑡)d𝑡 +
Where:
𝐾𝑝 : Proportional gain
𝐾𝑖 : Integral gain
𝐾𝑑 : Derivative gain
𝑒(𝑡): Target value
𝑢(𝑡): Output value
0
𝐾𝑑 d𝑒(𝑡)
d𝑡
Properties.
o Direction of the displacement. A positive address value indicates that the control
will change its initial state when its result is higher than the control point and will
have its initial state when it is lower. A negative address value will produce the
opposite behaviour. The control will change its initial state when its result are lower
than the control point and will have its initial state when it is higher.
o Allow a single change of state. When activating this option, the control can only
change state once in the simulation.
CYPEFIRE FDS / 74
o Initially activated. When activating this option, the control is activated at the
beginning of the simulation.
o Control point. It is the value of the control function where the control changes
state. Only functions that return a numerical value shou
ld be indicated.
3.15
Sections
The sections are entities of the FDS calculation engine that obtains the value of several
gaseous quantities in more than one point.
3.15.1.1
Description
•
Geometry. Indicates the measurement area as a plane perpendicular to one of the
global axes of the scene and can also be specified manually. The measurement area
can be a volume, a plane or a line.
•
Position. Indicates the height of the plane, if it is a plane perpendicular to the global
axes of the work, or if it is the limits of the measurement area.
3.15.1.2
Properties
•
Quantity of measurement. Indicates the quantity to be measured by the section.
•
General properties.
o Generate vectors. By activating this option, animated vectors will be generated that
can be visualized in Smokeview once the simulation is finished. If two sections are in
the same plane, this option should be activated in one of them. Otherwise, an extra
speed section will be generated.
o Obtain the data for
the centre of the cells. By default, the FDS calculation engine
calculates the results of the sections in the corners of the cells. When activating this
option, these values will be obtained for the centre of the cells.
CYPEFIRE FDS / 75
Fig. 68. Slice, description and properties
CYPEFIRE FDS / 76
4
Simulation
Once the introduction and definition of all the elements that make up the simulation of the
fire are complete, users can turn to this section.
4.1
Analysis/Calculation
CYPEFIRE FDS has different tools that help users solve this section using the Analysis/
Calculation that was created for the model.
4.1.1
FDS Report
Here, the reports that have been generated and contain defined characteristics of the
simulation can be obtained as a .fds file which can be read with any text editor.
Additionally, the route that the file is located can be viewed, as shown in the image below.
Fig. 69. FDS report
CYPEFIRE FDS / 77
4.1.2
Check errors
This tool is useful to activate befo
re beginning the simulation since it can take awhile for
the complete simulation to finish running. Therefore, if major errors are corrected before
the simulation, it can help the program perform a smoother analysis.
4.1.3
Smokeview
Smokeview is a tool designed to visually represent the data
obtained after analyzing the .fds file through the generated
project.smv file. When starting the Simulation in the main
toolbar, Smokeview will be launched automatically.
Smokeview is used before, during, and after the simulation
of the model. Smokeview can be used before starting the
simulation to verify that the model is correct (t = 0 s) and
during the calculation process to monitor the progress of
the simulation.
4.2
Fig. 70. Smokeview
Graphics
Once the simulation
is
finished,
the
graphs from the
main toolbar of the
program can be
accessed.
In these graphs, the
evolution of different
parameters that are
measured in the
simulation
(heat
Fig. 71. Graphics display, evolution of measured para
meters
released, heat by
radiation, heat by convection) can be observed, as seen in the following image, as well as
the operation of the devices and the controls introduced.
CYPEFIRE FDS / 78
Contact
How to setup a project, navigate through the user interface, design within the software,
and obtain results based off the design should be known after the completion of this
manual for CYPEFIRE FDS. If there are still questions, issues, or further information is
needed, please visit our website or contact CYPE. The contact information is below.
CYPE Ingenieros
Technical Support:
North America & United
Avda. de Loring, 4
support@cype.com
Kingdom Contact:
03003 Alicante - Spain
USA (+1) 202 569 8902
Tel. (+34) 965 92 25 50
UK (+44) 20 3608 1448
Fax (+34) 965 12 49 50
cype@cype.com
marketing@cype.com
www.en.cype.com
CYPE Italia
CYPE France
CYPE em Portugal (TOP
Tel. (+39) 06 94 803 504
Tel. (+33) 2 30 96 1744
Informática, Lda.)
Tel. (+39) 06 94 800 227
supporto.italia@c
meters
released, heat by
radiation, heat by convection) can be observed, as seen in the following image, as well as
the operation of the devices and the controls introduced.
CYPEFIRE FDS / 78
Contact
How to setup a project, navigate through the user interface, design within the software,
and obtain results based off the design should be known after the completion of this
manual for CYPEFIRE FDS. If there are still questions, issues, or further information is
needed, please visit our website or contact CYPE. The contact information is below.
CYPE Ingenieros
Technical Support:
North America & United
Avda. de Loring, 4
support@cype.com
Kingdom Contact:
03003 Alicante - Spain
USA (+1) 202 569 8902
Tel. (+34) 965 92 25 50
UK (+44) 20 3608 1448
Fax (+34) 965 12 49 50
cype@cype.com
marketing@cype.com
www.en.cype.com
CYPE Italia
CYPE France
CYPE em Portugal (TOP
Tel. (+39) 06 94 803 504
Tel. (+33) 2 30 96 1744
Informática, Lda.)
Tel. (+39) 06 94 800 227
supporto.italia@c
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