Comple plex x chemis mistr try y with h DARS Ka Karin Frjd - - PowerPoint PPT Presentation
Comple plex x chemis mistr try y with h DARS Ka Karin Frjd - - PowerPoint PPT Presentation
Comple plex x chemis mistr try y with h DARS Ka Karin Frjd Why DARS? S? Enabli bling ng det etai ailed led chem emistr try in your r CAE simul ulations ations Take e the righ ght desi sign gn choi oices ces, incl
Enabli bling ng det etai ailed led chem emistr try in your r CAE simul ulations ations
- Take
e the righ ght desi sign gn choi
- ices
ces, incl cluding ng chem emical al effec ects ts
- Fast
ster er and cheaper eaper desi sign cycles cles
- Evaluat
valuation
- n of enti
tirel rely new desi signs gns
Why DARS? S?
To capture ure chemica emical l effects ects Em Emissi sions
- ns
Ignit ition ion delay y times es Lamin minar r flame me speeds eds New w fue uels s & f fue uel l blends ends
Why comple lex chemis istr try? y?
Igniti tion dela lay y times s for diff ffere rent natu tural ral gas s quali liti ties Soot t surface face growth wth as funct ctio ion of mixtu ture re fract ction ion for r n- heptan tane comb mbust stio ion at variou ious s strain in rate tes
What is DARS? S?
4 Standalone ndalone softw tware are for r 0D and 1D analys yses es of chemical emical reacti ctions
- ns
Chem emist stry y analys yses Mecha hanism nism reduct ction ion Idealized ealized react ctor
- rs
– Ignition delay time – Emission production – Flame speed calculations
Libr brar ary y generati neration
- n
1D & 0D PDF mode dels s for in-cyl cylinde inder r combus mbusti tion
- n and
after ertr treatm tmen ent DARS ARS v2.10 0 releas ased! ed!
- Focus
s on libr brar ary gene neration tion fo for r STAR AR-CC CCM+ M+ an and STAR-CD CD
DARS
5
Impor mport t any mechani chanism sm in DAR ARS S Basic An Analys yse e the e chemist emistry y in react ctor
- rs
s and flames mes Un Under derst stand and reacti ction
- n pathways
ys throu
- ugh
gh species cies flow w analys ysis
Chemistr mistry analysi lysis
Igniti tion dela lay y times s as functi ction of tempe perat ature for n-he hepta tane n-hepta tane deco composit sitio ion CO producti ction in fuel rich ch combusti stion of n-hepta tane
n-he hepta tane ne comb mbusti tion,
- n, p=20
0 bar
Ignit ition n delay y times mes
Lamin minar ar flame me speeds eds
8
Laminar flame me speed as function tion of equival alenc nce rati tio and u unburned temperatu ture
Lamina nar flame e speeds eds with detail ailed ed chem emistr istry (291 species, ecies, 3081 1 reactio tions) ns) for a mixtur ure e of 95% iso-oc
- ctane,
ane, 5% n-hept eptane ane in air
Laminar flame me speed as function tion of unburned temperatu ture and p pressure
The laminar flame speeds generated by DARS can be used by the PCFM model in STAR-CCM+
Minor r speci cies
C2H2 CH2O HO2
Fuel l & main n species cies
CO2 CH4 CO OH
Soo
- ot
t for n-hep hepta tane ne combust mbustion, ion, p=50 bar
Emission ission mapping ing
NO for n-he hepta tane ne comb mbust stion, ion, p=50 bar
Emission ission mapping ing
CO for n-hept heptane ane combust mbustion ion, , p=50 0 bar
Emission ission mapping ing
To avoi
- id
d large e CPU times es the e mechani chanism sm can be reduc duced Mecha hanism nism reduct ction ion throu
- ugh
gh necess cessity ty analys ysis Visu sual al analys ysis is of the e reacti ction
- n sc
schem heme e throu
- ugh
gh flow w analys ysis Stea eady dy state e reduc ducti tion
- n through
- ugh life-ti
time me analys ysis s
Mechanism nism reducti ction
- n
Flow analysis for n-heptane decomposition
Mechanism nism Reducti ction
- n through
- ugh necess
ssity ty analysi ysis
Flow w + sensi nsiti tivi vity ty analys ysis s us used ed to det etect ect the e most t un unnecess necessary y sp species ies in the e mechani echanism sm Workflo kflow: – Read detailed reaction scheme – Run relevant reactor conditions, with necessity analysis turned on. – Let DARS remove species with necessity lower than your defined threshold value – Check mechanism validity through rerun of relevant reactor conditions 13 13
Mechanism reduction panel – choose reduction limit here DARS workbench – read mechanism, constant pressure and reduce mechanism modules
DAR ARS S standa ndard d chemis emistr try y mechanis chanisms ms
– n-heptane – TRF (n-heptane/toluene) – PRF (n-heptane/iso-octane) – Natural gas
Collab labora rati tion
- n with
h prof.
- f. Lu,
u, Un Univ. . of Conn nnecticut cticut
– n-dodecane – PRF (n-heptane/iso-octane) – Biodiesel – DME – Ethanol – Natural gas
An Any CHEM EMKIN KINTM
TM forma
rmatt tted ed mechanis chanism m from m litera rature re can be us used
Chemistr mistry mecha hanis nisms ms
Flow analysis for n-heptane decomposition
With h DAR ARS v2.10 0 you can expor port
– ECFM-3Z single/dual fuel libraries (STAR-CD) – ECFM-CleH single/dual fuel libraries (STAR-CD) – PVM-MF single/dual fuel libraries (STAR-CD) – FGM libraries (STAR-CCM+) – Soot libraries (STAR-CD and STAR-CCM+)
Straigh ightf tfor
- rward
d parame meter r sp speci cification, ication, designe gned d for each h librar ary y type
– Set up a full library calculation in less than 10 minutes.
Librar rary generat eration ion
Par Parallelliza ellizati tion
- n
Comma mmand nd line e execut cution ion of calcula ulati tions
- ns for
aut utomat mated ed workflo kflows ws
– Use the GUI to set up the calculation – Export case folders and files – Execute calculations from command line
- Run on clusters
- Automate workflow through scripting
Librar rary generat eration ion
Selection of number of processors to use in GUI ECFM-TKI library generation from command line
ECFM FM-3Z 3Z single/du gle/dual al fuel l librari raries es
DARS RS v2.10 0 can n export t ECFM-3Z 3Z TKI auto- igniti ition
- n librarie
aries for STAR AR-CD CD
– Constant pressure calculations using complex chemistry
Dual al fuel / single le fuel Specify fy rang nges es and nd grid in T, P, phi, EGR R and nd fuel fract ctio ion Librar ary y set et up ~ 10 min Librar ary y calcu cula lati tion
- n: ~ 3 h on 16 cores for singl
gle e fuel librar rary
17 17
Igniti tion dela lay y times s for straig ight t chain in hyd ydroca rocarbo rbon fuel l The gas s comp mposi siti tion panel, l, use sed for r speci cifi fica cati tion of para rame meter ter range and grid id
ECFM FM-CleH leH single/dua gle/dual l fuel l librari raries es
DARS RS v2.10 0 can n export t ECFM-CleH eH TKI aut uto- igniti ition
- n + Equi
uilibrium librium librar rarie ies for STAR AR-CD CD
– Constant pressure calculations + minimization
- f Gibbs free energy using complex chemistry
Dual al fuel / single le fuel Specify fy rang nges es and nd grid in T, P, phi, EGR R and nd fuel fract ctio ion Librar ary y set et up ~ 10 + 5 min Librar ary y calcu cula lati tion
- n: ~ 9 + 3 h on 16 cores
es for single le fuel librar ary
18 18
The e gas as compo positi sition
- n pan
anel, l, used sed for specif cifica icati tion of para ramete ter range and grid id CO equil ilibriu rium mass ss fracti ction as functi ction of equiva ivale lence ce rati tio and temperatu rature re
PVM-MF F singl gle/d e/dual ual fuel librari braries es
DARS RS v2.10 can expor
- rt
t PVM-MF MF librari braries es for r STAR AR-CD CD
– Constant pressure calculations using complex chemistry
Dual al fuel el / single ngle fuel el Speci ecify fy ranges nges and grid in T, P, phi, EGR and fuel el frac action tion Librar brary y set et up ~ 10 min Librar brary y calc lculat ulation:
- n: ~ 50 h on 16 cores
res for single ngle fuel el librar brary
19 19
The gas s composit sitio ion panel, l, use sed for r specif cifica icati tion
- f para
ramete ter range and grid id Igniti tion proce cess ss for n-hepta tane combusti stion at diff fferen rent t equiva ivale lence ce rati tios
FGM librari braries es
DARS RS v2.10 0 can n export t FGM librari aries es for STAR AR-CCM+ CCM+
– For non-premixed and partially premixed combustion – Constant pressure calculations using complex chemistry
Explore
- re combus
busti tion
- n of any
y fuel/o /oxidan dant t mixtu ture re
– Any CHEMKIN™ format chemistry can be used
Specify fy param ramet eter ers and nd grid in mixture ture fract ction
- n and
d heat t loss ratio tio Choose species for postproces
- cessing
ing in STAR AR-CCM+ Librar ary y set et up: ~ 10 min Librar ary y calcu cula lati tion
- n:
: ~ 15 min on 16 cores
20 20
The gas compo posi sition ion panel el, used d for
- r speci
cificat ication ion of param amet eters ers and grid id CO mass ss fract action ion during ing n-hep eptan ane e combu bust stion
- n at
variou ious s equival ivalen ence ce ratios
- s
Soot t source ce term rm librari braries es
DARS RS v2.10 0 can n export t Soot
- t section
- nal
al met ethod
- d librari
aries es for STAR AR-CD and d STAR AR- CC CCM+
– Flamelets are used to capture turbulence- chemistry interaction
Specify fy rang nges es and nd grid in T, P, EGR and d scalar lar dissipat ation ion rate Librar ary y set et up ~ 10 min Librar ary y calcu cula lati tion
- n: ~ 40 h on 16 cores
es for single le fuel librar ary
21 21
The gas s comp mposi siti tion panel, l, use sed for r speci cifi fication cation of paramete rameter r range and grid id Soot t surfa face ce growth wth as functi ction of mixtu ture re fracti ction for r n-hepta tane combusti stion at vario rious s strain rate tes
Readi dily ly available able libraries raries - diesel sel
Fuel Reference mixture Type Where to find Diesel 100% n- heptane EFCM-3Z TKI Contact support ECFM-CleH TKI + Equilibrium Contact support PVM STAR-CD v4.22 Soot Contact support 100% n- decane Soot STAR-CD v4.22 Diesel / natural gas dual fuel N-heptane / NG11 EFCM-3Z TKI Contact support ECFM-CleH TKI + Equilibrium Contact support n- heptane/meth ane PVM STAR-CD v4.22 Gasoline / diesel dual fuel PRF12 / n- heptane PVM Contact support
1 1 NG1:
meth thane 94.4 .40 % CO2 0.77 % N2 N2 1.37 % C2H6 3.46 46 %
2 2 PRF1
F1: Iso-octa ctane 95% n-hepta tane 5% 5%
Readi dily ly available able libraries raries – gasoli
- line
ne + o
- ther
er fuels ls
Fuel Reference mixture Type Where to find Gasoline PRF12 EFCM-3Z TKI STAR-CD v4.22 ECFM-CleH TKI STAR-CD v4.22 PVM STAR-CD v4.22 Flame speed STAR-CD v4.22 Soot STAR-CD v4.22 100% iso-
- ctane
Soot STAR-CD v4.22 TRF13 Soot STAR-CD v4.22 Gasoline / ethanol dual fuel TRF24 / Ethanol ECFM-3Z TKI STAR-CD v4.22 Laminar flame speed STAR-CD v4.22 PRF12/ E15 PVM Contact support Ethanol E15 PVM Contact support Natural gas methane PVM STAR-CD v4.22
2 2 PRF1:
F1: Iso-octa ctane 95% n-hepta tane 5% 5%
3 3 TRF1:
tolu luene 26 % iso so-octa ctane 60 % n-he hepta tane ne 14 4 %
4 4 TRF2:
tolu luene 45.4 .48 % iso-octa ctane 39.7 .75 % n-hepta tane 14.7 .77 %
5 E1:
1: Ethanol 99% Wate ter 1% 1%
DARS S – in in-cyli ylinder nder combustion ustion
- SI: two-zone stochastic model
- Knock
- Combustion
- Emissions
- DI: stochastic model with fuel
injection
- Combustion
- Emissions
- 10
- 5
5 10 15 20 25 30 0,0 20,0 40,0 60,0 80,0 100,0 0,0 0,2 0,4 0,6 0,8 1,0
Polynomials (4
th order)
Heat Release Exp Sim A, const. Sim B, f(CAD)
Crank Angle [deg ATDC] Rate of Heat Release [J/deg]
Mixing Time Sim A, const. (0.62ms) Sim B, f(CAD)
Mixing Time [ms]
DI SRM application – heat release rate. [Pasternak et al, SAE 2009-01-0676] SI SRM application – knock prediction. Lines are experiments, markers are calculations
Com
- mpar
aris ison
- n betw
etwee een n fue uels ls
– Effects of blending n-heptane with toluene (Fuel 2) vs. n- heptane (Fuel 1) – Effects of changes the initial pressure and temperature
Constant AFR Chemical effects due to varied EGR
Emission ission mapping ing
1D channel nnel mode del in DAR ARS Basic
– Thin film layer approach - transport to washcoat calculated – Surface chemistry in washcoat layer – Gas phase chemistry in gas – Detailed or global chemistry can be used. – Any CHEMKIN format chemistry can be used.
DARS S - cataly alyst st
washcoat Monolith wall
DARS S - cataly alyst st
DARS S - cataly alyst st
Save time by ana nalysing ysing chemica ical l reac acti tion
- ns in
1D before employin ying g full CFD
– Is detailed chemistry needed for the CFD calculation? – Can a reduced scheme be used? – Optimization of chemistry parameters for reduced schemes.
Study dy emission
- n conver
ersion
- n as func
ncti tion
- n of
– Catalyst length – Exhaust gas temperature – Exhaust species composition
For
– TWC – SCR – DOC – LNT – ...
28 28
200 400 600 800 1,000 1,200
- 30
20 70 120 170 220 Temperature [K] / Concentration (ppm) Time [min]
InletT[K] NO_GasOut NO2_GasOut N2O_GasOut NH3_GasOut
Ammo monia ia SCR R for a temper erature ramp C3H6 H6 inhibi bitio ion of NO oxidati idation
- n under
er lean an con
- ndit
ditio ions in Nox-stor
- rage
e catalyst talyst
NH NH3 SCR as fun uncti ction
- n of
inlet t ammonia monia conc ncen entrati tration
- n
Am Ammoni monia SCR for an ammonia monia ramp.
- mp. Inle
let t gas s compos posit ition: ion: 250 ppm NO, , 250 0 ppm NO NO2, , 8% O2, 5% H2O. Temperatu perature: re: 175⁰C Up Upper r panel: el: exper perim iment ent and si simul ulat ation ion by Chalme lmers. s. Lower r panel: el: DAR ARS simula ulati tion
- n
Applicat ication ion exam ample le – SCR SCR
29 29
0.00E+00 1.00E-04 2.00E-04 3.00E-04 4.00E-04 5.00E-04 6.00E-04 100 200 300 400 500 600 50 100 150 200 250 300 350 400
InletT[K] NO_GasOut N2O_GasOut NH3_GasOut NO2_GasOut
Time [min] Temperature [K] Molefraction
Application example –
- Full powertrain (including aftertreatment) emission
control
In-cylinder combustion
Three-way-catalyst (TWC)
Piping
Pressure trace for Φ= 0.98, 1.00, 1.02
Φ oscillation influence on mass fraction
- f CO in & out the pipe
TWC in inle let & outlet et CO and NO mass ss fract action ions, s, at Φ oscillat illation ion of 1 and 2 Hz
Fröjd jd K., Bjerkbo rkborn rn, , S., Perlma lman, C., Mauss, ss, F., DEER R 2011
Global bal chem emist stry y optimization imization Cataly lysis sis Libr brar aries ies for CFD D – new in D n DARS S v2.10! 0! Mecha hanism nism reduct ction ion Chem emist stry y analys ysis is
Summa mmary
... . to help p you u un under ersta tand nd and efficie icientl ntly y us use com
- mple
lex x chem emistr try
Thank k you for your r attention ention
Down wnload load DARS S v2.10 10 from
- m the Steve