I’ve started to explore the soot deposition function in FDS6. I was able to follow the example codes from the FDS User guide 'propane_flame_deposition' and successfully run a model using propane as a fuel.
However, I am having trouble running a model with polyurethane (chemical formula C6.3H7.1NO2.1) as the reaction fuel.
I have used the chemical equation balancer from Kris's website (http://www.koverholt.com/chemical-equation-balancer/) to determine the stoichiometric coefficients for polyurethane.
C6.3H7.1NO2.1 + 5.9391(O2 + 3.7619N2) --> 5.2141CO2 + 3.55H2O + 22.8421N2 + 1.0859C
Here are the REAC and SPEC lines using the equation above:
&SPEC ID = 'NITROGEN', LUMPED_COMPONENT_ONLY = .TRUE. /
&SPEC ID = 'OXYGEN', LUMPED_COMPONENT_ONLY = .TRUE. /
&SPEC ID = 'CARBON DIOXIDE', LUMPED_COMPONENT_ONLY = .TRUE. /
&SPEC ID = 'WATER VAPOR', LUMPED_COMPONENT_ONLY = .TRUE. /
&SPEC ID = 'POLYURETHANE' /
&SPEC ID = 'SOOT', AEROSOL=.TRUE. /
&SPEC ID = 'AIR', SPEC_ID ='NITROGEN','OXYGEN',
VOLUME_FRACTION = 3.7619,1.000, BACKGROUND = .TRUE. /
&SPEC ID = 'PRODUCTS', SPEC_ID ='NITROGEN','CARBON DIOXIDE','WATER VAPOR',
VOLUME_FRACTION = 22.8421,5.2141,3.55/
&REAC FUEL = 'POLYURETHANE', HEAT_OF_COMBUSTION=2270.,
SPEC_ID_NU = 'POLYURETHANE','AIR','PRODUCTS','SOOT',
NU=-1.,-5.9391,1.,1.0859/
When I try to running this input file, I get an error saying:
ERROR: Problem with REAC 1. Mass of products, 946.351 does not equal mass of reactants, 844.776
This tells me that the stoichiometric coefficients are incorrect, is there any chemistry guru out there that might be able to correctly balance this equation?
Any help would be greatly appreciated, thanking you in advance.
Kind regards,
Jaimee Choi
Exova Warringtonfire Aus
Try looking at the example given by Eq. (12.5) in the user guide, in Sec. 12.2 on Complex Chemistry.
In the way I think about lumped species, your NUs for Air and Products are wrong. You need to group the lumped species (like you did with the parens around the Air components) and normalize their coefficients to sum to unity. Then the coefficient outside the parens will be the correct lumped species NU.
I am confused by several of the examples given in the user guide, including the propane soot deposition case.
Craig or Jason: I know you internally normalize the mass fractions for the lumped species definitions. But do you then also correct the NUs? This needs to be clarified in the guides. I see no mention of it between giving the correct specification of a lumped species reaction balance (12.5) and subsequent simplistic representations.
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