CFD Online Logo CFD Online URL
www.cfd-online.com
[Sponsors]
Home > Forums > General Forums > Main CFD Forum

Interphase mass transfer of a reaction

Register Blogs Community New Posts Updated Threads Search

Reply
 
LinkBack Thread Tools Search this Thread Display Modes
Old   May 15, 2017, 22:42
Post Interphase mass transfer of a reaction
  #1
Member
 
Shuai Wang
Join Date: May 2017
Location: TaiYuan.China
Posts: 30
Rep Power: 9
cfx_ws1992 is on a distinguished road
i am trying to make interphase mass transfer achieve a decomposition reaction.
1.set up reaction:
REACTION: Reaction 1
Option = Single Step
COMBUSTION MODEL:
Chemical Timescale = 1.37E-4 [s]
Option = Finite Rate Chemistry
END
FORWARD REACTION RATE:
Option = Expression
Reaction Rate = HydrateRate
END
PRODUCTS:
Materials List = CH4,Water
Option = Child Materials
CHILD MATERIAL: CH4
Option = Stoichiometric
Stoichiometric Coefficient = 1.0
END
CHILD MATERIAL: Water
Option = Stoichiometric
Stoichiometric Coefficient = 6
END
END
REACTANTS:
Materials List = hydrate
Option = Child Materials
CHILD MATERIAL: hydrate
Option = Stoichiometric
Stoichiometric Coefficient = 1.0
END
END
END
END
2.set up reaction energy:
BULK SOURCES:
Option = Use Volume Fraction
EQUATION SOURCE: energy
Multiply by Porosity = Off
Option = Source
Source = HeatSource
END
END
3.set up interphase mass transfer:
FLUID PAIR: Gas | Hydrate
INTERPHASE HEAT TRANSFER:
Heat Transfer Coefficient = 5 [W m^-2 K^-1]
Option = Heat Transfer Coefficient
END
INTERPHASE TRANSFER MODEL:
Option = Particle Model
END
MASS TRANSFER:
Option = Specified Mass Transfer
SPECIFIED MASS TRANSFER:
Fluid1to2 Mass Flux = GasMassFlow
Option = Interfacial Mass Flux
END
END
MOMENTUM TRANSFER:
DRAG FORCE:
Drag Coefficient = 4
Option = Drag Coefficient
END
LIFT FORCE:
Option = None
END
VIRTUAL MASS FORCE:
Option = None
END
WALL LUBRICATION FORCE:
Lubrication Coefficient C1 = -0.01
Lubrication Coefficient C2 = 0.05
Option = Antal
END
END
END
FLUID PAIR: Gas | Water
INTERPHASE HEAT TRANSFER:
Heat Transfer Coefficient = 0.6 [W m^-2 K^-1]
Option = Heat Transfer Coefficient
END
INTERPHASE TRANSFER MODEL:
Interface Length Scale = 1. [mm]
Option = Mixture Model
END
MASS TRANSFER:
Option = None
END
MOMENTUM TRANSFER:
DRAG FORCE:
Drag Coefficient = 4
Option = Drag Coefficient
END
END
END
FLUID PAIR: Hydrate | Water
INTERPHASE HEAT TRANSFER:
Heat Transfer Coefficient = 50 [W m^-2 K^-1]
Option = Heat Transfer Coefficient
END
INTERPHASE TRANSFER MODEL:
Option = Particle Model
END
MASS TRANSFER:
Option = Specified Mass Transfer
SPECIFIED MASS TRANSFER:
Fluid1to2 Mass Flux = WaterMassFlow
Option = Interfacial Mass Flux
END
END
MOMENTUM TRANSFER:
DRAG FORCE:
Drag Coefficient = 4
Option = Drag Coefficient
END
LIFT FORCE:
Option = None
END
VIRTUAL MASS FORCE:
Option = None
END
WALL LUBRICATION FORCE:
Option = None
END
END
END
4.error:
ERROR #001100279 has occurred in subroutine ErrAction.
Message:
Floating point exception: Multiple faults


| ERROR #001100279 has occurred in subroutine ErrAction.
| Message:
| Stopped in routine FPX: C_FPX_HANDLER

Thanks for anyone who gives me a view.
cfx_ws1992 is offline   Reply With Quote

Reply


Posting Rules
You may not post new threads
You may not post replies
You may not post attachments
You may not edit your posts

BB code is On
Smilies are On
[IMG] code is On
HTML code is Off
Trackbacks are Off
Pingbacks are On
Refbacks are On


Similar Threads
Thread Thread Starter Forum Replies Last Post
Radiation in semi-transparent media with surface-to-surface model? mpeppels CFX 11 August 22, 2019 08:30
mass flow in is not equal to mass flow out saii CFX 12 March 19, 2018 06:21
mass transfer in ANSYS thipps ANSYS 1 August 29, 2013 12:05
Determining the mass transfer reaction? Lindz Fluent UDF and Scheme Programming 0 September 30, 2009 09:36
additional variable mass transfer in CFX5.6 john CFX 1 February 14, 2004 01:30


All times are GMT -4. The time now is 12:35.