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Yiguang Ju Princeton University Plasma Assisted Combustion & Chemical Conversion 2021. 6. 21 Princeton Combustion Summer School

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Page 1: Plasma Assisted Combustion & Chemical Conversion

Yiguang Ju

Princeton University

Plasma Assisted Combustion & Chemical Conversion

2021. 6. 21

Princeton Combustion Summer School

Page 2: Plasma Assisted Combustion & Chemical Conversion

Sang Hee Won

Associate professor,

Univ. South Carolina

Joseph Lefkowitz

Research fellow

AFRL

Wenting Sun

Assistant professor,

Georgia Tech

Prof. Richard B Miles

Princeton/Texas A.M.

Prof. Christophe Laux

Ecole Centrale Paris

Aric Rousso

Graduate student

Timothy Ombrello,

Senior research

engineer

AFRL

Prof. Igor V. Adamovich

Ohio State University

Prof. Svetlana Starikovskaya

Ecole Polytechnique

Dr. Andrey Starikovskiy

Princeton

Acknowledgement

Prof. Bruce Koel

Princeton Univ.

Prof. Haibao Mu

XiAn Jiaotong

Visiting

Timothy Chen

Graduate student

Xingqian Mao

Princeton

Prof. Min Suk Cha

KAUST

Prof.Qi Chen

Beijing Jiaotong

Visiting

Hongtao Zhong

Princeton

Chao Yan

Princeton

Dr. Nils Hansen

Sandia National Lab

Dr. Chris Kliewer

Sandia National Lab

Annemie Bogaerts

Univ. Antwerp

Page 3: Plasma Assisted Combustion & Chemical Conversion

Low carbon energy conversion: From Fossil Fuel Energy to Electron Energy:

Fossil fuels

High carbon

• Power• Fuels• Chemicals• Fertilizers (NH3)• Materials • E-fuels• H2

• Energy storage…

Low carbon

CO2Electricity

Electrons

Catalysis

Plasma/photons

Hot flame

Cool flame

N-heptane/He

O2/He

BiomassPhotons Low efficiency

Higher efficiency Energy storage

EVs

eCO2

• Transformation of fossil energy industry to low carbon chemical manufacturing industry.

• Development of plasma assisted advanced engines

Syngasl

Page 4: Plasma Assisted Combustion & Chemical Conversion

Te >> Tv>>Tn

Non-Equilibrium plasma

Te ≈ Tv ≈ Tn Near Equilibrium plasma

arc

Gliding arc

Corona

Tn~n*10,000 K

Tn~n*1000 K

Tn~n*100 K

Te > Tv>Tn

What is plasma?

4

Plasma: 4th state of matter: A partially ionized, quasi-neutral charged reactive mixture…

Page 5: Plasma Assisted Combustion & Chemical Conversion

Energy transfer and active species production in Non-Equilibrium Plasma

6

Photoionization

Slow heating (ms)

5

High energy electrons/ions (ns) Fast heating (ns)

Active species (ns)

Non-equilibrium

Equilibrium

Electronically excited species

Vibrationally excited species

Temperature rise (ms)

• Thermal effect (μs-ms)• Chemistry effect (ns-ms)

Page 6: Plasma Assisted Combustion & Chemical Conversion

Plasma

Advanced engines Nano materials

Electrode

Electrode

CO2, CH4 → CnH2n

Fuel/NH3 synthesis

+

-Pollutants control

AgricultureBiochemical……

Plasma-Chemistry: a new pathway to Low Carbon Electron Energy

Chemistry & Dynamics

Page 7: Plasma Assisted Combustion & Chemical Conversion

1. Introduction and plasma discharge

2. Plasma Assisted Combustion and Applications in Engines

3. Effects of plasma on ignition, flame propagation, minimum ignition energy, and cool flames

4. Effects of electric field on combustion: Joule heating and ionic wind

5. Plasma chemistry and kinetic studies

6. In situ laser diagnostics

7. Thermal-chemical instability and chemical mode analysis

8. Modeling of plasma assisted combustion and chemical conversion

9. Perspectives of future researchReview papers of plasma assisted combustion and chemical conversion1. Ju, Y. and Sun, W., 2015. Plasma assisted combustion: dynamics and chemistry. Progress in Energy and Combustion Science, 48, pp.21-83.2. Starik AM, Loukhovitski BI, Sharipov AS, Titova NS. 2015 Physics and chemistry of the influence of excited molecules on combustion

enhancement. Phil. Trans. R. Soc. A 373: 20140341. 3. Igor V Adamovich and Walter R Lempert, 2015, Challenges in understanding and predictive model development of plasma-assisted

combustion, Plasma Physics and Controlled Fusion, Volume 57, Number 1.4. Starikovskiy A, Aleksandrov N. Plasma assisted ignition and combustion. Prog. Energy Combust. Sci. 2013;39:61–110.5. Starikovskaia SM. Plasma assisted ignition and combustion. 2006; J. Phys. D: Appl. Phys. 39:R265–R299.6. CO Laux, TG Spence, CH Kruger, RN Zare, Optical diagnostics of atmospheric pressure air plasmas, Plasma Sources Science and Technology 12

(2), 1257. A Fridman, S Nester, LA Kennedy, A Saveliev, O Mutaf-Yardimci, Gliding arc gas discharge, Prog. Energy Combust. Sci. 25 (2), 211-231 8. Bogaerts, A., et al., 2020. The 2020 plasma catalysis roadmap. Journal of Physics D: Applied Physics, 53(44), p.443001.9. Ju Y, Reuter CB, Yehia OR, Farouk TI, Won SH. Dynamics of cool flames. Progress in Energy and Combustion Science. 2019 Nov 1;75:100787.

Lecture contents and review articles

7

Page 8: Plasma Assisted Combustion & Chemical Conversion

Milestones of Plasma assisted combustion

1860 Étienne Lenoir used an electric spark plug in his gas

engine, the first internal combustion piston engine.

(Spark ignitor for engines)

1814 – W.T. Brande. Phil.Trans.Roy.Soc, 104, 51. (Electric field-flame interaction)

1948, Calcote, 3rd Symposium on Combustion and Flame, and Explosion

Phenomena (Vol. 3, No. 1, pp. 245-253) (Ionic wind)(a) XH2,PJ = 0.3, PIN = 3.0 kW, PIN total = 4.3 kW

(b) XH2,PJ = 0.5, PIN = 6.0 kW, PIN total = 8.2 kW

1981: Kimura, L, et al., Combustion and Flame, Vol. 42, No. 3,

pp. 297- 305 (Plasma jet in supersonic combustion)

2013: Leonov, S.B., Firsov, A.A., Shurupov, M.A., Michael,

J.B., Shneider, M.N., Miles, R.B. and Popov, N.A., 2012.

(laser guiding plasma discharge/fs-ps diagnostics)

1998: Starikovskaia, S.M., Starikovskii, A.Y. and Zatsepin, D.V., Journal of

Physics D: Applied Physics, 31(9), p.1118. ]Anikin N B and Marchenko N 2005

(Nanosecond discharge).

2014: Won, S.H., Jiang, B., Diévart, P.,

Sohn, C.H. and Ju, Y., Proc. Comb Inst.

(Plasma assisted cool flames and LTC)(a) Hot flame (b) Cool flame

2019: Zhong, Shneider, Ju, 2019.

(Plasma thermal-chemical instability)

2020s (Plasma catalysis?)

Page 9: Plasma Assisted Combustion & Chemical Conversion

How does plasma enhance combustion?

Ju and Sun: Plasma assisted combustion, Progress of Energy & Combustion Science, 2015

New reaction pathways with fuel

Plasma discharge

Temperature

increase

Thermal

Radicals

Int. species

Ions/electrons

Excited

species

Kinetic

Fuelfragments

Transport

Ionic windInstability

NO, O3

O, H, OH

N2*, N2(v)

O2 (a1Δg)

H2 , CO

CH4

CH2O

Combustion Enhancement

O2+, N2

+

T0 B, E Le, Rc

O(1D)

Large Ignition VolumePlasma instabilityTurbulence

Excited states

Page 10: Plasma Assisted Combustion & Chemical Conversion

Mild Combustion

Cool Flames

Fuel/CO2

Reforming

New enginetechnology

Scramjet/ RDE engines

LowEmissions

Plasma assisted combustion

Applications of plasma assisted combustion

10

• Materials synthesis• Plasma medicine• Plasma cleaning• Plasma water treatment• …

Page 11: Plasma Assisted Combustion & Chemical Conversion

• Thermal plasma (Equilibrium) Tgas ~ 2000K-20000KHot plasma: Ttrans = Trot = Tvib = Te Example: (Arc, lightening)

2. Plasma Discharges

Temperature:

• Non-thermal (Non-Equilibrium plasma) Tgas ~ 300K-2000KCold plasma: Ttrans = Trot < Tvib < Te

Low pressure – DC, RF glow discharges

Atmospheric pressure – DBD, Microwave, Corona & Micro-plasmas

Frequency: DC, AC, RF (MHz), MW(GHz), Pulsed…

Discharge processes:

Discharge types:

Electric field, streamer, Corona, glow, arc

Electron-beam, Corona, Dielectric barrier discharge (DBD),

gliding arc, arc, micro discharge, surface discharge…

Plasma: A partially ionized, quasi-neutral charged mixture

in which electrons and ions are separately free.

11

Page 12: Plasma Assisted Combustion & Chemical Conversion

------

++++++

++++++

++++++

------

------

++++++

++++++

++++++

------

------

------

Perturbation of a neutral plasmaTotal charge number: 𝑄 = 𝑒𝑉𝑛𝑒Electric field (between two slabs): E=

𝑄

𝜀𝐴=𝑒𝑉𝑛

𝑒

𝜀𝐴=

𝑒𝑛𝑒

𝜀x

Coulomb force on an electron: F=-eE=−𝑒2𝑛

𝑒

𝜀𝑥

x

Equation of electron motion: F=mea 𝑚𝑒

𝑑2𝑥

𝑑𝑡2= −

𝑒2𝑛𝑒𝜀

𝑥

The frequency of electron plasma oscillation is: 𝜔𝑝 =𝑒2𝑛

𝑒

𝑚𝑒𝜀=9000 𝑛𝑒 (Hz)

Plasma frequency

If the electron density is 109 cm-3 , thefrequency is about 300 MHz. Therefore,plasma is very fast to restore chargeneutral properties.

ωp

The electron plasma frequency is critical to the propagation of electromagnetic wave in plasma. If

the electromagnetic wave frequency (ω) is less than ωp, ω<ωp, electrons in the plasma will response

and extracts energy from the electric field and reflect the incident wave. If ω>ωp, electrons in

plasma can not response and the electric field will transmit through the plasma without reflection.

Therefore, for a given ω, there is a critical plasma electron number density (cm-3), ne,c:

ω

2

2

,e

mn

ep

ce

At microwave frequency of 2.45 GHz, if the electron density is 9×1010 cm-3 , ωp =2.7GHz > ω=2.45Gz, microwave will not penetrate to the interior of the plasma, but reflect on the plasma surface within a small length scale.

ε:permittivity

V: volume

ne: electron number density (cm-3)

e: electron charge

12

E

Perturb

Page 13: Plasma Assisted Combustion & Chemical Conversion

Mean free path and collisional frequency

d u

A

B

Mean free path

λ

nd v :unit timeper number collision The 2

Mean free path:

the mean free path

ndvnd

u22

2

1

time unit per collisions of number

time unit per distance traveling

For electron neutral molecule collisions in weakly ionized gas, ndudn

u

e

ene 22,

4

)4/(

25210 105.2)105.3(2

1

m=0.075

T=300K, p=1 atm, Molecule diameter: d=3.5A0, the molecule number density:

325

23

5

/105.23001038.1

10013.1m

319 /10 cm=2.45

Collision frequency

u: mean velocityv: relative mean velocityd: neutral particle diameter

e

eBneene

m

Tkndu

8

4/

2

,,

,8

)(0

m

Tkduuvfu B

sec/107.610075.0/500/: 96 ufrequencyCollison c

2 :areasection Cross d

2uv

n=p/(kBT)=

13

Page 14: Plasma Assisted Combustion & Chemical Conversion

• Plasma shielding effect: If one inserts a perturbing charge objective (Q)

into a neutral plasma, as the free charges move towards a perturbing

charge objective (Q). The perturbing electric field effect will be

neutralized in a characteristic distance of D. D is the Debye length.

Debye Shielding and plasma sheath

+

E~0

E>0

+Q+

+

+

++

+

+

+

+

+

+

+

+

+

+

D

++

+

-- - - -

Cathode (perturbing objective)

++

+ + + ++

D

Ion bombardment

Sheath

Neutral plasma

Potential distribution

How large is Debye length? 14

Page 15: Plasma Assisted Combustion & Chemical Conversion

𝛻 ∙ 𝑬 =𝑒

𝜀(ni-ne)In the Maxwell’s equation:

For a steady state problem:

ε: the permittivity of the plasma

𝑬 = −𝛻𝜑 𝛻𝟐𝝋 = −𝑒

𝜀(ni-ne)

𝛻𝟐𝒆𝝋

𝒌𝑩𝑻𝒆= −

1

λ𝑫𝟐(ni

n0-ne

n0)

λ𝑫 =𝒌𝑩𝑻𝒆𝜀

n0𝑒2

In air, if Te = 1000K and n0 = 1013 cm-3,

we have λ D = 6.9 × 10−5 cm= 6.9 × 10−7 m.

Debye length

• Therefore, when L >> λD and there is enough electrons in the Debye sphere

to produce shielding, plasma will be almost quasi-neutral everywhere.

• The equation means that the net charge potential will decrease exponentially in a length scale of λ D

+

E~0

E>0

+Q+

+

+

++

+

+

+

+

+

+

+

+

+

+

D

++

Debye length

15

ε0 of a vacuum) :

8.85 x 10-12 (Faraday/m)

N𝒆 = n𝒆𝟒𝝅

𝟑𝝀𝑫𝟑 >> 1

• Response time of plasma shielding to recover quasi-neutrality

in plasma :𝜏𝐷~

λ𝐷

𝑣𝑒=

λ𝐷

𝑘𝐵𝑇𝑒/𝑚𝑒= 1/𝜔𝑝

Page 16: Plasma Assisted Combustion & Chemical Conversion

16

If the plasma response time (τD) is shorter than the characteristic time of an

external electromagnetic field: τD < τp (such as laser, nanosecond pulse discharge, microwave), then this

radiation will be shielded out, otherwise, will be refractively transmitted.

2014 Paul Gibbon, CERN School on Plasma Wave Acceleration

𝜔𝑝2

𝜔2 =𝑒2𝑛𝑒𝜀𝑚𝑒

λ2

4𝜋2𝑐2

λ: laser wavelengthc: light speed

shielded outTransmission

Page 17: Plasma Assisted Combustion & Chemical Conversion

tc

t

nne

B

ei

EjB

BE

B

E

2

1

0

)(

E: electric field, B: magnetic fieldj: currentε: permittivity μB: permeability

)n -e(n v)n - e(n )vn - ve(n eeiieieeii VVj

Maxwell equation

Diffusion with an external electric field: diffusion velocity and drifting velocity

E

E

eeeeee

iiiiii

nnDVn

nnDVn

Di Charge diffusivities,

μi electron and ion mobilities

For weakly ionized plasma: ni << n; ne << n

eBe

e

Bi

i

Tk

e

D

Tk

e

D

Einstein relation

ii v v V

Mean + relative velocity

17

ee v v V

Question: can the ions and electrons diffuse independently?

Page 18: Plasma Assisted Combustion & Chemical Conversion

field electricambipolar : )(

)(-

eie

eie

n

nDD

E

Ambipolar diffusion (steady state neutral plasma)

In one-dimensional plasma (zero flow velocity): The ion and electrons fluxes are,

In steady state and quasi-neutral plasma:

iambi

eii

iieiiii

iiiie

nD

n

nDDnnD

nnD

)(

)( -

- i

ETherefore:

E

E

eeeeeee

iiiiiii

nnDVn

nnDVn

ei

)1( )(

)(

i

eie

e

ii

ei

ieeiambi

T

TDDD

DDD

)( ei

In non-equilibrium plasma, Te is much greater than Ti, the ambipolar diffusivity is much higher than ion diffusivity.

18

Page 19: Plasma Assisted Combustion & Chemical Conversion

Energy transfer and active species production in Non-Equilibrium Plasma

6

Photoionization

Slow heating (ms)

19

High energy electrons/ions (ns) Fast heating (ns)

Active species (ns)

Non-equilibrium

Equilibrium

Electronically excited species

Vibrationally excited species

Temperature rise (ms)

• Thermal effect (μs-ms)• Chemistry effect (ns-ms)

Page 20: Plasma Assisted Combustion & Chemical Conversion

Figure 1. Experimental and predicted temperature and N2

vibrational temperature during and after a ns pulse

discharge in air between two spherical electrodes 1 cm

apart at 100 Torr.

Figure 2. Experimental and predicted temperature during and

after a ns discharge pulse in an H2-air mixture (ϕ=0.14) between

two spherical electrodes 0.9 cm apart at 40 Torr, plotted together

with predicted number density of electronically excited N2

molecules and Tv(N2).

Igor V Adamovich and Walter R Lempert, 2015, Challenges in understanding and predictive model development of plasma-assisted combustion, Plasma Physics and Controlled Fusion, Volume 57, Number 1.

Energy transfer in Plasmas: fast heating and slow heating (vibrational relaxation)time-resolved and spatially-resolved measurements of N2 vibrational temperature

Two-step thermalization

20

Page 21: Plasma Assisted Combustion & Chemical Conversion

-10 0 10 20 30 40 5010

12

1013

1014

1015

1016

1017

0

1

2

3

4

5

6

0

50

100

150

200

250

300

Time (ns)

N2(A)

N2(C)

Ab

so

lute

de

nsitie

s [

cm

-3]

N2(B)

02.0x10

17

4.0x1017

6.0x1017

8.0x1017

1.0x1018

1.2x1018

O (3P) density

1500

2000

2500 from N

2(C-B)

from N2(B-A)

Te

mp

era

ture

[K

]

Temperature

0

10

20

30

40

Cu

rre

nt [A

]

Vo

lta

ge

(V

)

V Iconduction

E/N

[T

d]

Timescales of plasma chemistry

hheating =21±5%

hdiss. = 35±5%

Ultrafast heating:

900 K in 20 ns

Ultrafast

dissociation of O2

Rusterholtz et al, J. Phys.D, 46, 464010, Dec 2013

Plasma chemistry occurs in nanoseconds! Christophe Laux, 2014

Page 22: Plasma Assisted Combustion & Chemical Conversion

Ionization processes: Thermal ionization, electron impact ionization, photo-ionization for second electrons

Plasma and Plasma Properties

e + O2= 2e + O2+ (electron-impact)

hν + O2= O2+ + e (photon ionization)

M+O2= M+O2++ e (Thermal)

e + O2= O2-

e + O2+=O(3P) + O(1D)

Electron quenching processes: recombination and attachment

+

x d0

Plasma temperature: Electron temperature, vibrational and rotational temperatureElectron temperature: 1 eV = 11600 K = 1.6 ×10−19 Joules.E/N: Townsend, E: V/m; N: 1/m3; 1Td=10-21 V/m2

Second electron

Equilibrium and non-equilibrium plasma:Equilibrium: Distribution function: Boltzmann

Non-equilibrium: Distribution function: non-Maxwell-Boltzmann distribution

)/exp(),,1(.

TkgVEQ Bi

i

i

𝜕𝑓

𝜕𝑡+ 𝒗 ∙ 𝛻𝑓 −

𝑒

𝑚𝑬 ∙ 𝛻𝑣𝑓 = 𝐶 𝑓

Temperature: Te ≈ Tv ≈ Tn

Temperature: Te >> Tv>>Tn 22

Page 23: Plasma Assisted Combustion & Chemical Conversion

Te >> Tv>>Tn

Non-Equilibriumplasma

Te ≈ Tv ≈ Tn Near Equilibrium plasma

arc

Gliding arc

Corona

Tn~n*10,000 K

Tn~n*1000 K

Tn~n*100 K

Te > Tv>Tn

A few examples

23

Page 24: Plasma Assisted Combustion & Chemical Conversion

Electron impact avalanche𝑑𝑛

𝑒

𝑑𝑥= α𝑛𝑒

𝑛𝑒=eα𝑥

α: The 1st Townsend coefficient, inverse of net ionization length scale. It is determined exponentially by E/p or E/N (electric field strength)

If α > 0, electron avalanche phenomenon.

α = 𝐴𝑝𝑒𝑥𝑝 −𝐵𝑝

𝐸𝑛𝑒

A,B: constantsE: electric field p: pressurene: electron number density

+

x d0

Breakdown voltage:

The minimum voltage between two electrodes that causes an arc. At the breakdown voltage, the rates of ionization and dissociative attachment becomes equal.

Paschen's law: pdmin=1 torr cm. The nonlinear dependence of breakdown voltage is

to due to electron impact avalanche via collisioinal energy transfer

Lieberman, Michael A.; Lichtenberg, Allan J. (2005)

The breakdown field for atmospheric air~28.7 kV cm−1

Mean free path (1 atm, air): Molecules: 0.1 µm, Electron-molecule: 5.5 µm

pdmin=1 torr cm at 760 Torr, dmin=13.2 µm, twice of the mean free path.

Few

co

llisi

on

More collisions

How to produce uniform plasma at high pressure?24

Page 25: Plasma Assisted Combustion & Chemical Conversion

Meek and Loeb criterion: Streamer is formed once the total number of electrons in the electron avalanche is so large that their space charge field becomes comparable to E0, the avalanche-to-streamer transition occurs. α𝑑~18 − 20 and ne= 1013 cm-1

Stream propagation: A space charge wave, which can penetrate into neutral gas

with a velocity much higher than the electron drift velocity, up to a fraction of the

speed of light.

anodecathode

--

++

ℎν

E

+-

Streamer

- +

α𝑑~18 − 20

Positive streamer

E0

neutral

Space chargeStreamer head

+

Power input by external field: N0𝑞𝑒𝐸0𝑉𝑠Power consumed in ionization:

𝑑𝑛0

𝑑𝑡𝑄𝑒

Plasma DischargesStreamer discharge: a non-thermal narrow filamentary discharge channels formed at the initial stage of a sparkbreakdown by a high voltage pulse (1-100 ns). A streamer has a streamer head (space charge) with a high reduced electricfield (~100 Td, 5-10 kV cm−1 for air at atmospheric pressure) followed by a streamer channel with lower electric field andhigher conductivity (charge number density). Formation of a streamer discharge occurs when the electric field in thestreamer head is at the same magnitude or greater than a critical external electric field (4.4 kV cm−1 in air at atmosphericpressure for a positive streamer, 8–12.5 kV cm−1 for negative streamer). Streamers are fundamental components in manykinds of discharges such as the dielectric-barrier discharges, corona discharge, and spark. It is widely used in industrialozone production, biomedical treatment, plasma assisted combustion, pollution control. Note: a microwave streamer is ahot plasma not a streamer.

Energy balance:

25

Page 26: Plasma Assisted Combustion & Chemical Conversion

Fig. (a) Geometry of the simulation domain. (b) Propagation of growing and decaying positive streamers in an external field of10 kV cm−1. Both positive streamers are initiated from a Gaussian distributed plasma cloud with a peak density of 1020 m−3 and acharacteristic size σ0 of 0.05 mm. The radius of the spherical electrode Rsph is 0.5 mm. The only difference is that in the left panelthe spherical electrode has a potential Usph = 3.5 kV, whereas in the right panel Usph = 3.2 kV. (c) Propagation of negativestreamers in an external field of 20 kV cm−1. For both negative streamers, the initial plasma cloud has a peak density of 1018 m−3and a characteristic size of 0.10 mm. The electrode radius Rsph = 1.0 mm, and in the left panel Usph = 4.0 kV, whereas in the rightpanel Usph = 3.4 kV

Qin et al., J. Phys. D: Appl. Phys. 47 (2014) 435202 (9pp)

Flame front: auto-ignition and diffusive heat transfer, self-supported propagationStreamer: ionization and space charge transfer, external field supported propagation

Positive and negative streamers: Propagation of negative streamer requires a much stronger space charge field.

Streamer propagation vs. Flame propagation

26

Page 27: Plasma Assisted Combustion & Chemical Conversion

Corona DischargeAn discharge around a highly curved conducting electrode induced by a high electric field, but the

external electric field is not high enough to cause a breakdown or arc. Widely used in ozone generation.

Positive corona: electrons are attracted to curved positive electrode and have enough energy to cause

electron avalanche. Electron energy is high, density is low.

Negative corona: ions are attracted to curved negative electrode. The photon emissions via ion-

bombardment on electrode surface cause electron avalanche. Electrons have lower energy but higher

density.

Fig. Pulsed corona discharge and positive streamer development: CCD photos of the point-wire discharge in air using 5μs optical gate. Applied voltages: (a) at

7.5 kV, (b) and (c) at 12.5 kV. For (a) and (b) the semiconductor switch is used, for (c) the spark gap. The electron temperature is about 5-10 eV. By E M van

Veldhuizen and W R Rutgers, J. Phys. D: Appl. Phys. 35 (2002) 2169–2179 PII: S0022

(a) (b) (c)

27

Page 28: Plasma Assisted Combustion & Chemical Conversion

A discharge that occurs between electrodes with at least one electrode is covered by dielectric materials. It is a corona

discharge with a dielectric electrode. The existence of dielectric barrier limits the current and restricts transition of DBD

discharge to arcing. DBD discharge often has filamentary micro discharge structures and is physically behaving like an

incomplete streamer breakdown. DBD discharge has low electron number density and high electron energy and been widely

used in ozone generators.

Dielectric barrier discharge (DBD) and NS DBD

Rectangular quartz channel 22 mm x 10

mm in cross-section and 280 mm in

length. Rectangular copper electrodes, 15

x 60 mm. High-voltage pulses 20 kV on

the high voltage electrode, 25 ns duration

at the half-amplitude, up to 20 KHz.

Nanosecond DBD discharge in air: 20 kV, 10 kHz, pulse N10. Left:

Front view; Right: side view

Conclusion: NS discharge in DBD geometry in air is non-uniform. Initial electrical

field’s distribution and thermal ionization instability development form the non-

uniform energy distribution in the discharge. This non-uniformity can play a key

role in kinetic experiments in this type of the discharge.Andrey Starikovskiy et al., 2014, AIAA-paper

40 Torr/AR, NS BDB

28

Page 29: Plasma Assisted Combustion & Chemical Conversion

DC Glow Discharge (high special uniformity and volumetric)

The glow discharge is stable in a low pressure, but it is possibleto stabilize such a plasma at atmospheric pressure if threerequirements are met: (i) use of a source frequency of over 1kHz, (U) insertion of a dielectric plate (or plates) between thetwo metal electrodes, (iii) use of a helium dilution gas.

A self sustained weakly ionized volumetric (non-filamentary) discharge supported by thesecondary electron emission from the cathode. Ithas three distinctive structures: Negative glow,Faraday dark space, and positive column.

http://en.wikipedia.org/wiki/File:Electric_glow_discharge_schematic.png

Princeton Plasma Physics Laboratory

29

Page 30: Plasma Assisted Combustion & Chemical Conversion

5FIG. 2. 10 ns exposure time photograph of the gap taken when

the discharge current is maximum. The gap length is 5 mm and

the cathode is located at the bottom.

Cathode is at the bottom

FIG. 1 100 ns exposure time photographs of the gap taken during the discharge initiation, the discharge current being

periodic. The number on the current wave form a) corresponds to the number on the left side of the picture b) and indicates

the time when the picture was taken. The gap length is 5 mm. In each picture, the cathode is located at the bottom. Francoise

Massines et al., J. Appl. Phys., Vol. 83, No. 6, 15 March 1998

Positive column

Faraday dark space

Negative glow

30

Page 31: Plasma Assisted Combustion & Chemical Conversion

Atmospheric pressure DC glow discharge

Figure 2. Images of glow discharge in atmospheric

pressure air at (a) 0.1 mm, (b) 0.5 mm, (c) 1mm

and (d) 3mm electrode spacing

Figure 3. Image of the glow discharge in atmospheric

pressure hydrogen. Positive column and negative glow

are visible. In addition standing striations are visible in the

positive column.

David Staack, Bakhtier Farouk, Alexander

Gutsol and Alexander Fridman, Plasma

Sources Sci. Technol. 14 (2005) 700–711

31

Page 32: Plasma Assisted Combustion & Chemical Conversion

•Rotational temperature (Trot) increases with vibrational temperature (Tvib) decreases with increase in pressure.• Above 100 psi, they are measured to be within 500K of each other which is equal to the uncertainty in Tvib fitting.

David Staack, UTAM

Transition from micro glow discharge to equilibrium arc discharge

32

Page 33: Plasma Assisted Combustion & Chemical Conversion

Spark Discharge

A small volume, high temperature, and high current equilibrium arc initiated by ahigh voltage breakdown discharge (~10 ns). It has high current (1-1000 A), lowvoltage (10-100 V), and low electron temperature (~1 eV). Spark discharge iswidely used in gasoline engines. The role of spark discharge is to create hightemperature environment for ignition. Laser ignition is also to create a spark.

Plasma torch

Meghnad Saha derived an equation for the relative number of atoms ineach ionization state in an equilibrium plasma:

Tk

EE

Be

ie

i

i

i B

ii

eh

Tkm

gn

g

n

n

12/3

2

11 22

It depends on the number density of electrons, ne. This is because as the number density of electrons increase, the electric field decreases and thus lower the ionization state.

Plasma torch is also a continuous electric arc. It is high temperature nearequilibrium plasma. It is widely used in ignition and materials processing.The temperature, power, and electron number density is very high. Itmostly places a thermal effect in dissociating reactants and acceleratingchemical reactions.

33

Page 34: Plasma Assisted Combustion & Chemical Conversion

Fig. 1 Left: Schematic of a traditional gliding arc plasma discharge with

the numbers corresponding to the sequence in time evolution of the arc as

it moves along the electrodes (Ombrello and Ju). Right: direct image of a

gliding arc time trajectory [Courtesy from Dr. Z.S. Li at Lund University].

Fig. 3 Short exposure grayscale photograph of the

magnetic gliding arc discharge once stabilized at the

largest gap, with the cathode spot (CS) and positive

column (PC) shown.

Fig. 2 Pictures of the gliding arc plasma system with the (a) side view of central

electrode, (b) top view of system, and (c) time integrated top view photograph of

the magnetic gliding arc creating a plasma disk to quasi-uniformly activate the

flow. The numbers in (a) and (b) indicate the path of the gliding arc from

initiation, point 1, to arc rotation/elongation, points 2 and 3, and final arc

stabilization, point 4.

a gliding non-equilibrium electric discharges invented by Lesueur et al. [1]. The main distinctive aspect of the gliding

arc is a high level of non-equilibrium with both high electron temperature (1-2 eV) and high electron density as well as

high gas temperature (~2000 K). It can be inexpensively generated under near-to-atmospheric pressures.

[1]. H. Lesueur, A. Czemichowski and J. Chapelle, Frenchpatent 2 639 172.

[2] A Fridman, S Nester, LA Kennedy, A Saveliev, O Mutaf-Yardimci, Gliding arc gas discharge, Prog. Energy Combust. Sci. 25 (2), 211-231

Gliding arc

[3] Ombrello et al., AIAA Journal 2006. 34

Page 35: Plasma Assisted Combustion & Chemical Conversion

)1()()(1 2ET

r

TTr

rr

2

)/exp(/)( 0

2

0

2 TkET BElectrical conductivity.

0

2

00 /)(16)(2 ETkTr

TTrW B

IWlRIV /0

),4/(,2/

),2/(),4/(

2

00

0

2

0

RVWVV

RVIWRVl

critcrit

critcrit

,

)4/(2 2

00 WlRVVWRI

WE Electric field:

Energy conservation equation

Temperature: T

Effective electric field strength: E0

Conductive arc heat loss per unit length from above equation:

From Ohm’s law:

RWlRVVI 2/)4( 2

00 We have:

Corresponding to steady and unsteady gliding arc.

042

0 WlRVCritical condition:

35

RI

V=Wl/I

V0

Page 36: Plasma Assisted Combustion & Chemical Conversion

(a)

Fig. 2 Left: Plot of the increase in electric field in plasma after the transition point in a gliding arc discharge [8]. Right: three sequentialframes of gliding arc images recorded by a high-frame-rate camera, showing the conversion from a glow-type discharge to a muchbrighter spark-type discharge [7]. (Courtesy from Dr. Z.S. Li at Lund University)

Gliding arc voltage

36

Page 37: Plasma Assisted Combustion & Chemical Conversion

Short-cut

Gliding arc dynamics and radial production

Fig. 3 Left: A short-cut event recorded at 20 kHz framing rate using an exposure time of 13.9 μs. The short-cut current path is indicated by the arrow in the frame of t

= 50 μs. Right: Three typical single-shot OH PLIF images of a gliding arc using an exposure time of 2 µs, at two flow rates (a) 17.5 SLM, (b) 42 SLM. The typical

thickness of the OH distribution is labelled in the images with unit of centimeters [6, 7] (Courtesy from Dr. Z.S. Li at Lund University)

Magnetic gliding arcs

37

Page 38: Plasma Assisted Combustion & Chemical Conversion

RF and Microwave discharges

In DC and AC discharges, electrical power is delivered to plasma by moving electrons/ions to the electrodes across the cathode and anode sheaths. When the electrical frequency is very high like RF and MW, the time required for charge particles to move across the sheath becomes comparable or longer than the wave period of electrical field. Therefore, the interaction between electrical field and plasma is exclusively by charge displacement current, not by a directed current to electrodes. Therefore, it can be delivered without requirement of an electrode in contact with plasma by a sheath.

RF discharge (10k-100M Hz) Microwave discharge (1G-300G Hz)

p pe cmn )107( 110

Low pressure-1 atmField wavelength: metersLower electron energy (1-2 eV)Some sheath

Low pressure-high pressureField wave length: 12.24 cm at 2.45 GHzHigher electron energy (5-15eV)No high voltage sheath

• Inductive coupling: via oscillating magnetic field• Capacitive coupling: via oscillating electric field

RF & MW plasma coupling

Particle interaction Collective interaction

38

Page 39: Plasma Assisted Combustion & Chemical Conversion

microwave resonator

Qiang Wang et al, APPLIED PHYSICS LETTERS 104, 074107 (2014)

Miles et al., PrincetonIkeda et al., Imagineering Inc.

Microwave discharge for ignition and flames

39

Page 40: Plasma Assisted Combustion & Chemical Conversion

Micro-discharge 1

Microscale Discharges in Liquids

Microdischarge between ceramic

spheres (Tomohiro Nozaki, 2015)

Applications• Largescale surface ignition• Crude Oil Fuel Reforming• Medical Treatments• Plasma catalysts• Aerodynamic Control• High pressure materials processing

40

Electrode

Electrode

Preliminary tests of single (top) and four channels (bottom) micro-discharge using single a RF power supply.

The channel is 76mm Χ 26 mm with a gap distance about 0.5 mm, (Princeton, 2017)

Courtesy by David Staack

Microscale Discharge micro tips

Micro-discharge in CH4/He250 torr (Princeton, 2017)

Page 41: Plasma Assisted Combustion & Chemical Conversion

41

Nanostructured discharge

Parallel Plate electrodes Dielectrics(Al2O3 of 0.6 mm with AAO AAO film of 50 μm, holes of 200nm p= 60Torr d= 1 inches rf power =1~100W

α to ϒ discharge mode transition is observed Under α discharge mode, dielectric materials has small

effect on the discharge Under ϒ discharge mode, the discharge on AAO area is

difficult to transit from α to ϒ mode than Al2O3

Possibility of plasma control using nanostructures

Haibo Mu and Yiguang Ju, 2017, unpublished work

Findings

Page 42: Plasma Assisted Combustion & Chemical Conversion

eaiee nDn

dt

dn 2)(

Breakdown condition of plasma discharge

eaiee n

Dn

dt

dn

2

)(

electrons oflength diffusion sticcharacteri:

tD

ee

ai

enn)(

02

2

)/()/(

D

NENEai

Breakdown condition:

ec

e

c m

eTvvlD

3

8

33

1 2

Electron production, attachment, and diffusion:

Diffusivity of electrons (no Ambipolar diffusion):

Introducing a diffusion length scale:

Electron production, attachment, and diffusion:

νi: ionization rate, νa: attachment rate

42

Page 43: Plasma Assisted Combustion & Chemical Conversion

43

Plasma thermal instability

Lightening arc

Streamer-leader transition

Gallimberti [1979, 2002] Bazelyan et al. [2007]

Positive feedback between Joule heating and electric field.

δT↑

δN ↓δ(E/N) ↑ δTe ↑

δne ↑ δ(jE) ↑ T: gas temperature

N: gas number density

E/N: reduced electric field

Te: electron temperature

ne: electron number density

jE: Joule heating

Red Sprites, Blue Jets and Elves

http://www.albany.edu/faculty/rgk/atm101/sprite.htm

Page 44: Plasma Assisted Combustion & Chemical Conversion

44

Air pollution helps wildfires create their own lightning

Science, 2021 doi:10.1126/science.abj6782Nikk Ogasa

How do we explain this and how to control plasma discharge?

Pulse 50

150

200

300

450

600

Pulse 50

150

200

300

450

600

Stoichiometric 2.8% C5H12, 22.2% O2, 75% Ar Dilution

Aric Rousso et al., Plasma Sources Science and Technology, 2020

Page 45: Plasma Assisted Combustion & Chemical Conversion

Electron energy and number density in various Equilibrium & Non-equilibrium Various Plasmas

1010 1015

0.1

1

10

Ele

ctr

on

te

mp

era

ture

, e

V

Electron number density, 1/m3

Corona DBD

Arc

Flame MHD

RF

Glow

Nanosec

0.1

1

10 Corona DBD

Gliding Arc

Arc/Spark

Flame MHD

DC, MW

Micro dis.

45Ju and Sun: Plasma assisted combustion, Progress of Energy & Combustion Science, 2015

Page 46: Plasma Assisted Combustion & Chemical Conversion

46

Table 1: LTPs examples used in modern plasma

applications: Te, Ti, Tg, Tnp are the effective

temperatures (or mean energy) of electrons,

ions, gas, nanoparticles, respectively. Ne, Nnp are

the densities of electrons and nanoparticles,

respectively. εI is the ion energy. Z is the

ionization degree defined as the ratio of the

plasma density to the sum of atomic, molecular,

and plasma densities. Abbreviations: APPJ

(atmospheric pressure plasma jet), DBD

(dielectric barrier discharge), ExB (crossed

electric and magnetic fields)

Yevgeny Raitses, 2019

Non-equilibrium Low Temperature Plasma (LTP) Properties

Page 47: Plasma Assisted Combustion & Chemical Conversion

47

What are our questions?

CombustionPlasma

Chemistry

PhysicsInstability Catalysis

Page 48: Plasma Assisted Combustion & Chemical Conversion

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2. Plasma Assisted Combustion and Chemical Conversion

Yiguang Ju

1. PAC in scramjet engines and detonation engines

2. PAC in spark ignition engines

3. PAC in flame stabilizations for gas turbine engines

4. PAC in ignition, combustion, cool flames, and emission control

5. Plasma assisted chemical conversion: CH4/CO2 and NH3

Yiguang Ju, Princeton University

Princeton Combustion Summer School

2021.6.21

Page 49: Plasma Assisted Combustion & Chemical Conversion

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MotivationDevelopment of High Speed/Low Emission Power Systems & Synfuels

•Enhanced combustion efficiency and flame stability

•Predictive new engine design with alternative fuels for low emissions

Advanced Gas Turbines

(Low NOx, after burner, renewable fuels)

Ignition and Flame Stabilization

Internal combustion engines:

Ignition timing control

Conventional discharge?

Pulse Detonation Engines

Ignition and DDT

Page 50: Plasma Assisted Combustion & Chemical Conversion

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1. PAC for Ramjets and Scramjets

Flow Residence Time

Chemical Reaction Time<< 1

•Flow time scale <1 ms

Mach 10

X43: Hydrogen

Silane: ignition enhancer

X-51 (AFOSR)

• Mach 4-8

• Hydrocarbon fuels

(JP-8, JP-7)

Difficulty in ignition, flame stabilization, and

combustion completion

Page 51: Plasma Assisted Combustion & Chemical Conversion

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Increase residence time or reduce combustion time

Solutions:

•Cavity

•Oblique shocks

Niioka et al.1998

•Plasma

Takita et al.

Kimura et al. 1981

Masuya et al. 1993

Page 52: Plasma Assisted Combustion & Chemical Conversion

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Combustion lab.

Plasma-Assisted Combustion

Ignition & Flame speed ~(a, Dfuel, , Φ, Rc, e , …)Tf-Ea

Plasma discharge

Temperature

increase

Thermal Enhancement

Radicals

Ions/electrons

Excited

species

Kinetic enhancement

Fuelfragments

Transport enhancement

Ionic wind

O, NO

N2 *(A)

O2 (a1Δg)

H2, CH4

C2H4

O2+

Mixing, flow

Page 53: Plasma Assisted Combustion & Chemical Conversion

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Combustion lab.

O Radical Production by Plasma on ignition and flame extinction

Takita and Ju (2006)

He/O2 = 0.45:0.55 He/O2 = 0.38:0.62

Effect of PAC on methane flame ignition and extinction, Sun W. et al. 2010, 2011

Page 54: Plasma Assisted Combustion & Chemical Conversion

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(a) XH2,PJ = 0.3, PIN = 3.0 kW, PIN total = 4.3 kW

(b) XH2,PJ = 0.5, PIN = 6.0 kW, PIN total = 8.2 kW

Fig. 2.1 H2 ignition by plasma torch in a M=2.3 flow and the

effect of total heat addition on pre-combustion shock wave, XH2

is hydrogen mole fraction in H2/N2 plasma torch; Pin: plasma

torch electric power, Pin total: total heat addition (Pin+H2 enthalpy

flux) [192]

Electron-impact reactions (CH4, O2, N2, H2)

e + CH4 = CH4++2e

e + CH4 = CH3 + H + e

e + O2 = 2O + e

e + N2 = 2N + e

N+O2 = NO+N

NO + HO2 = NO2 + OH

:

Pyrex Glass Window

30

Plasma

Torch

x

yPlasma

Jet

320

170

Main Stream

Fuel Injector

z

30

Nozzle

M=1.8

Feedstock

Pyrex Glass Window

30

Plasma

Torch

x

yPlasma

Jet

320

170

Main Stream

Fuel Injector

z

30

Nozzle

M=1.8

Feedstock

Effect of mixing ratio of N2/O2 feedstock on wall pressure

increase due to combustion of fuel injected at Xi = 24 mm in

experiment, H2/air mixture, Takita, Abe, Masuya, and Ju,

2006,

Plasma jet ignition enhancement

Page 55: Plasma Assisted Combustion & Chemical Conversion

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Combustion lab.Fig. 2.2b Direct photographs of DBD plasma in M=2.0

supersonic flow [181]

Fig. 2.2a Schematic of the test section with

DBD and plasma torch [181]

DBD/plasma jet ignition

Wall pressure distributions when H2 fuel was injected

from xi = −40 mm under simultaneous operations of

DBD device and PJ torch. (a) Pin = 1.75 kW.

(b) Pin = 2.4 kW. (c) Pin = 3.3 kW. (d) Pin = 4.05 kW.

Page 56: Plasma Assisted Combustion & Chemical Conversion

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Fig. 2.4 Schematic of the cavity model [182]Fig. 2.5 OH PLIF images of a cavity flame in supersonic flows

of two different enthalpies: (a) without the plasma and (b) with

plasma at M=2.9, Jn~4 of H2 jet, and (c) without plasma and

(d) with plasma at M=2.6 Jn~3.5 of H2 jet [182]

A nanosecond pulsed plasma discharge, arc jet vitiated

ignition

0.15

0.48

1.95

2.72

0.93

1.34

2.26

3.51

N2 arc jet heated air free stream: T0 = 2,500 K, P0 = 1

bar, M=4.5

ISO 200, Exp. 3

ms

Cavity

Equivalence

ratio

1)

Partially-

Premixed

Flame

2) Cavity

Flame

Holding

3) Non-

Premixed

Flame

Arc jet vitiated ignition, Do et al. 2013

Page 57: Plasma Assisted Combustion & Chemical Conversion

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Fig. 2.6 Schematic of experimental setup and electrodes arrangement

[184]

Fig. 2.7 Left: discharge without fuel injection.

Right: discharge interaction with H2 injection [184]

Gliding arc flame stabilization

large volume and forced ignition

Page 58: Plasma Assisted Combustion & Chemical Conversion

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Combustion lab.Esakov et al. AIAA-paper-2005

I. Esakov et al., IEEE TRANSACTIONS ON PLASMA SCIENCE, VOL. 37,

NO. 12, DECEMBER 2009

Subcritical streamer microwave discharge

The discharge in the undercritical field can be initiated,

for example, at the location of a cylindrical MW

vibrator in the EM beam. Conditions of local electrical

breakdown E ≥ Ecr in this case are realized at the

ends of the vibrator.

vibrator

Page 59: Plasma Assisted Combustion & Chemical Conversion

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Microwave flame stabilization in a high speed flow (200 m/s) as a

preburner

Precombustor

Fig. 2.9 Schematic of experimental setup [186]

Van Wie et al., AIAA 2006-1212

cylindrical MW vibrator

Page 60: Plasma Assisted Combustion & Chemical Conversion

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Fig. 2.22 Left: A valve less PDE setup at the Naval Postgraduate School. This type of architecture requires a

booster and its anticipated applications are missiles or rockets. Right: Comparison of ignition delays for C2H4/air

mixture using spark plug and transient plasma igniter [178]

Fig. 2.23 (a) PDE engine facility at the Air Force Research Lab at Wright-Patterson Air Force Base, (b) Schlieren imaging of nanosecond pulsed

discharge igniter in CH4/air mixture, Φ=1, (c) Schlieren imaging of nanosecond pulsed discharge igniter in CH4/air mixture, Φ=0.8 [62]

Plasma assisted ignition and DDT in PDE/RDE

0

1

2

3

4

5

6

7

1 10 100 1000

Fla

me

-De

ve

lop

me

nt

Tim

e [

ms

]

Total Energy [mJ]

MSD

NRP discharge, f = 1-5 kHz

NRP discharge, f = 10-40 kHz

Page 61: Plasma Assisted Combustion & Chemical Conversion

Figure 3: Ignition kernel development for 5

pulses of 3.2 mJ per pulse. Left images:

pulse repetition frequency of 2 kHz. Right

images: pulse repetition frequency of 40

kHz.

0.01 ms

0.5 ms

1.0 ms

2.0 ms

4.0 ms

6.0 ms

2 kHz 40 kHz

0

200

400

600

800

1000

1200

1400

1.E-8

1.E-6

1.E-4

1.E-2

1.E+0

1.E+2

0 0.05 0.1 0.15 0.2 0.25

Te

mp

era

ture

Mo

le F

rac

tio

n

Time (ms)

O atom, 5 kHz O atom, 10 kHzO atom, 40 kHz T, 5 kHzT, 10 kHz T, 40 kHz

a.

Figure 6. a) Computed atomic oxygen concentration and temperature

as a function of time with 1% oxygen dissociation repeated at 5 kHz,

10 kHz, and 40 kHz frequencies for stoichiometric methane-air

mixtures at 850 K. b) . Computed atomic oxygen concentration and

temperature as a function of time with 0.1%, 0.5%, and 1% oxygen

dissociation repeated at 40 kHz frequency for stoichiometric

methane-air mixtures at 850 K.

• Increase of ignition kernel volume• Reactivate chemical radicals before quenching

Lefkowitz, J.K., Guo, P., Ombrello, T., Won, S.H., Stevens, C.A., Hoke, J.L., Schauer, F. and Ju, Y.,

2015. Combustion and Flame, 162(6), pp.2496-2507.

Page 62: Plasma Assisted Combustion & Chemical Conversion

Plasma assisted DDT for PDE/RDE

15

• Control of detonation formation in pressure gain engines

Detonation failure

Kawasaki, A et al, 2019. Proceedings of the

Combustion Institute, 37(3), pp.3461-3469.

Pratt and Whitney Rocketdyne (PWR)

Page 63: Plasma Assisted Combustion & Chemical Conversion

16

No Ozone

Ozone

Kinetic Effect of Ozone Addition on DDD of C2H2/O2 Mixtures in A Microchannel

Sepulveda, J., et al., AIAA journal, 57(2), pp.476-481. DOI: 10.2514/1.J057773

Plasma may enhance DDT ?

Page 64: Plasma Assisted Combustion & Chemical Conversion

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Pressure SensorThermocouple

Air Flow Sensor

Carburetor

Throttle Rod Choke Rod

Exhaust

2. PAC for IC engines

PU-Imagineering Inc.

SP-HCCI/RCCI

Page 65: Plasma Assisted Combustion & Chemical Conversion

Challenge: Development of 60+ % Efficient Engines

Gross thermal efficiency ~ 42.3%

Heat loss ~ 54.6%

Carnot efficiency ~ 1-300/2100=86%

Otto efficiency: 68%

18

Diesel engines

Diesel engine (Nissan)

Output

Efficiency of lean burn gasoline engine

SIP program in Japan, 2019

We need low temperature combustion (LTC)

• Lean burn• Ignition assisted LTC engines like

HCCI (homogenous charge compression ignition)

RCCI (Reactivity controlled compression ignition)

• Higher compression ratio, Const Vol. comb.• Green fuels …

Page 66: Plasma Assisted Combustion & Chemical Conversion

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Combustion lab.Gundersen et al., 2003

Transient corona discharge

Disk electrode & streamers

Corona enhanced ignition

Page 67: Plasma Assisted Combustion & Chemical Conversion

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Fig. 2.19 Left: streamers generated by a single 370 mJ, 56 kV, 54 ns pulse

(maximum E/N~400 Td) in air (10 s gate time); Right: flame propagation from

multiple ignition sites at the base of the streamers after a single pulse in F=1.1

C2H4/air mixture (1 ms gate time) [81]

Fig. 2.20 Images of flame development in F=1.1 C2H4/air mixture, 6 ms after ignition. A 300 ms gate

time was used with equal sensitivity for both images and 996×990 resolution. Left: spark ignition

using a standard 105 mJ, 10 ms, 15 kV spark ignition system and a spark plug with a 1 mm gap. Right:

transient plasma ignition using a 70 mJ, 12 ns, 54 kV pulse with a 6 mm gap [81]

1. Shiraishi T, Urushihara T, Gundersen MA. A trial of ignition innovation of gasoline engine by nanosecond

pulsed low temperature plasma ignition. J. Phys. D: Appl. Phys. 2009;42:135208.

Page 68: Plasma Assisted Combustion & Chemical Conversion

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Microwave and nanosecond plasma assisted ignition

Nanosec pulses

Less

Heat Loss

Larger

volume

t1 t2

O, OH, NO, C2H4… production

Microwave

Spark Large

heat

Loss,

Small

volume

t1 t2

Fig.1 Current spark ignition plug: large heat loss, small volume

microwave repetitive nanosecond ignition with radical production,

Increased volume, less heat loss

Page 69: Plasma Assisted Combustion & Chemical Conversion

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Spark, Microwave, Gliding arc

Microwavepulsed power

generator

Synchronizationpulse

generator

Gliding arc power generator

Nanosecond pulsed plasma

generator

Microwave antenna(Imaging Eng. Inc)

SparkMGANSDelectrodes

OH* Comparison between Spark and MW ignition.

Imagineering Inc.

Page 70: Plasma Assisted Combustion & Chemical Conversion

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Ikeda et al., Imagineering Inc.

Page 71: Plasma Assisted Combustion & Chemical Conversion

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Fig. 2.16(a) direct photograph of plasma assisted 34 cc Fuji engine test setup and (b) the comparison of

limits of stable engine operating conditions with and without microwave (MW) discharge at 2000 rpm [69] .

Lefkowitz, J.K., Ju, Y., Tsuruoka, R. and Ikeda, Y., 2012. A study of plasma-assisted ignition in a small

internal combustion engine. AIAA paper-2012-1133.

Page 72: Plasma Assisted Combustion & Chemical Conversion

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Combustion lab.Q Wang et al., Applied Physics Letters 103, 204104 (2013); doi:

10.1063/1.4830272

Spark plug

ignition (Φ)

Microwave

ignition

1 bar >2 1.6

2 bar 1.8 1.0

4 bar 0.9 0.7

6 bar 0.9 0.7

8 bar 0.9 0.7

Table 1. The lean burn limits at different initial pressures

The pressure curve of MW ignition at 8 bar

Microwave/spark ignition

Page 73: Plasma Assisted Combustion & Chemical Conversion

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Fig. 2.13 The effect of spark ignition and microwave enhanced spark ignition on COVIMEP, fuel consumption and exhaust

emission [172]

Fig. 2.14 the SI and SI+MW modes as a function of equivalence ratio at an initial pressure of 1.08 bar and

300 K (a) for FDT, (b) for FRT [70]

Fig. 2.12 Comparison of C3H8 flame images

in a compression-expansion engine using

conventional spark plug and microwave

enhanced spark plug, F=1, initial pressure 600

kPa, initial engine speed 600 rpm [172]

Microwave/spark ignition in engine

Page 74: Plasma Assisted Combustion & Chemical Conversion

Fig. 2.11 Comparison of ignition using spark plug (left), microwave

(middle), gliding arc (right) (Photos were provided by Knite Inc. and

Imagineering Inc.) [197]

Ignition to flame transition(critical radius, Rc)

Flame Radius, R

Fla

me

Pro

pa

ga

ting

Sp

ee

d,U

10-1

100

101

102

10-2

10-1

100

101

Q=0.0

Q=0.1

Q=0.15

Q=0.6

(a), Le=1.2, h=0.0

a

b

cd

e

f

g

h

i

j

Critical ignition radius

Rc

Q?

Role of plasma:

• Mainly increase the initial ignition volume,

Rc; not increase flame speed!

• The thermal effect is not very large.

Why do we see a significant extension of lean burn in engines with microwave?

Page 75: Plasma Assisted Combustion & Chemical Conversion

Ignition by nanosecond surface dielectric barrier discharge (SDBD)

S M Starikovskaia, J. Phys. D: Appl. Phys. 47 (2014) 353001 (34pp)

S.A. Stepanyan, M.A. Boumehdi, G. Vanhove, P. Desgroux, N.A. Popov, S.M. Starikovskaia, Comb. & Flame, 162 (2015) 1336-1349

600 650 700 750 800 850 900 950 10006

8

10

12

14

16 (CH4:O2, =1) + 76% Ar

(n-C4H

10:O

2, =1) + 76% Ar

(n-C4H

10:O

2, =1) + 76% N

2

(CH4:O2, =0.3) + 75% Ar

(CH4:O2, =0.5) + 75% Ar

No autoignition

Pre

ssu

re P

d,

atm

Temperature Tc, K

S M Starikovskaia

Page 76: Plasma Assisted Combustion & Chemical Conversion

29

Dissociation and fast gas heating via

electronic excitation of molecular nitrogen

0 500 1000 1500 2000

500

1000

1500

2000

2500

U=10 kV, T=20 ns

1.5 mm ID, 80 mm length

Tem

pera

ture

, K

Time, ns

Capillary ns discharge in air,

P=25 Torr, T0=300K

N2 + e -> N2 (C3Pu) + e

N2 (C3Pu) + O2 -> N2 + O + O(1D)

O. Dutuit, N. Carrasco, R. Thissen et al. 2012 The Astrophysical J. Suppl. Series, 204/2

N. Popov, 2011, J. Phys. D: Appl. Phys. 44, 285201 (16pp)

Page 77: Plasma Assisted Combustion & Chemical Conversion

0 50 100 150 200

0

10

20

30

40

Plasma assisted ignition, U=-24 kV

PTDC=14.7 atm

TC

=972 K

discharge

initiation

(blue step)

Pre

ssu

re,

atm

Time, ms

30

Autoignition vs plasma ignition in RCM

at PTDC=15 bar and TC=970 K, (CH4:O2)+76%Ar

0 50 100 150 200

0

10

20

30

40

PTDC=14.7 atm

TC

=972 K

Pre

ssu

re,

atm

Time, ms

Autoignition

E=0.1-5 mJ, 100 “kernels”

S.A. Stepanyan, M.A. Boumehdi, G. Vanhove, P. Desgroux, N.A. Popov, S.M. Starikovskaia, Comb. & Flame, 162 (2015) 1336-1349

Page 78: Plasma Assisted Combustion & Chemical Conversion

31

Pressure trace and corresponding fast

imaging of flame propagation

200 205 210 215 2200

5

10

15

20

25

30

35

40

discharge

initiation

Pre

ss

ion

/ b

ar

Time / ms

0.8 ms 1 ms 1.2 ms 1.4 ms

1.6 ms 1.8 ms 2 ms

Pressure detector

CH4:O2, ER=1 + 70% Ar, TC=947 K, PTDC=15.4 bar

S.A. Stepanyan, M.A. Boumehdi, G. Vanhove, P. Desgroux, N.A. Popov, S.M. Starikovskaia, Comb. & Flame, 162 (2015) 1336-1349

Page 79: Plasma Assisted Combustion & Chemical Conversion

32

Experiments in n–C7H16:O2:N2

Autoignition (black) and plasma ignition (red)

100 200 300 400

0

1

2

3

4

5P

TDC=2,3 bar

TC=646 K

V = 46 kV

Pre

ss

ure

, b

ar

Time, ms

No discharge

With discharge

Discharge initiation

100 200 300 400

0.0

0.4

0.8

1.2

1.6

Pre

ss

ure

, b

ar

Time, ms

No discharge

With dischargePTDC

=1,6 bar

TC=648 K

V = 46 kV

Discharge initiation

The discharge is able to modify gradually a cool flame

(U increase or P increase) and to initiate a 2-stage flame

Page 80: Plasma Assisted Combustion & Chemical Conversion

33

Polarity: U>0

Energy deposition

W= 4.8 mJ

Quasiuniform ignition around HV electrode. Streamer discharge. Pressure 6 bar, Temperature 300 K.

Second regime of ignition:

Ignition along the

perimeter of HV electrode

Flame Initiation in H2/Air ER=0.5, P=6 bar

S.A. Shcherbanev, N.A. Popov, S.M. Starikovskaia, Comb. & Flame, 176 (2017) 272-284

Page 81: Plasma Assisted Combustion & Chemical Conversion

34

Polarity: U>0

Energy deposition

W= 12 mJ

Ignition along the channels. Filamentary discharge. Pressure 6 bar, Temperature 300 K.

Third regime of ignition:

Ignition along the

discharge channels

Flame Initiation in H2/Air ER=0.5, P=6 bar

S.A. Shcherbanev, N.A. Popov, S.M. Starikovskaia, Comb. & Flame, 176 (2017) 272-284

Page 82: Plasma Assisted Combustion & Chemical Conversion

Pri

nce

ton

Un

iver

sity

Combustion lab.

Fig. 2.21 Direct photograph of a prototype laser igniter

showing breakdown in air at multiple points [200]

Controlled plasma discharge for volumetric ignition

1

cm

(a)

(b)

(c)

Laser ignition and laser guided

discharge control, Miles et al. 2013

Fig. 3.16 Arc produced flow instability and jets [238]

Page 83: Plasma Assisted Combustion & Chemical Conversion

Is low temperature combustion (LTC) relevant to engines?

36

TimescalesLow temperature ignition 0.1-1 msGasoline/diesel engine (30 CAD) 5 msGas turbine engine 1-5 msTurbulence eddy, l/u’ 0.1-100 msFlame time scale, δ/ub 0.1-1ms

Skeen et al. 2015

n-dodecane spray

Plasm assisted cool flame ignition

CH2O

Rainer N. Dahms et al., Proceedings

of the Combustion Institute 36 (2017)

Page 84: Plasma Assisted Combustion & Chemical Conversion

37

Prometheus bringing fire to the earth

History of flame discovery: 3 different flames

1M B.C. 1817

FoodTools

Industrial revolutions

Space Exploration

2000 2010 2012-2013 2015 2017-2019

New enginesNew fuels

Premixed flames

Page 85: Plasma Assisted Combustion & Chemical Conversion

Lean flame stabilization demonstrations

• MINI-PAC Bluff-body stabilized flame (propane or methane, 1 bar, 11 kW)

• TWO-STAGE SWIRLED INJECTOR (Propane air, 1 bar, 52 kW)

• AERODYNAMIC INJECTOR (MERCATO, Kerosene/air, 3 bar, 200 kW)

38

10

0m

m

• LEL: reduced by 10%

• Plasma power = 75 W

• LEL: reduced

from 0.4 to 0.11

• Plasma power = 300 W

• LEL: reduced from 0.44 to 0.21

• Plasma power = 1 kW

Page 86: Plasma Assisted Combustion & Chemical Conversion

Pri

nce

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Un

iver

sity

Combustion lab.Laux et al., 2007

Nanosecond discharge on fuel lean flame stabilization

Page 87: Plasma Assisted Combustion & Chemical Conversion

Plasma aided Ammonia Combustion

40J. Choe, W. Sun, T. Ombrello, C. Carter, “Plasma assisted ammonia combustion: Simultaneous NOx reduction and flame

enhancement.” 2021 Combustion and Flame, 228, 430-432.

(a) Schematic of the experimental setup, and direct photographs (ISO100, F/10, 2 s) of flames

(b) no plasma, ϕ=0.94 (c) with plasma, ϕ=0.94, (d) no plasma, ϕ=0.71 (c) with plasma, ϕ=0.71

Page 88: Plasma Assisted Combustion & Chemical Conversion

Extension on LBO and Decreased NOx

41

(a) lean blowoff limits of ammonia/air flames with and without plasma,

(b) NOx emissions without and with plasma (ϕ = 0.94)

Plasma extended lean blowout (LBO) limits of ammonia flame and

simultaneously decreased NOx formation. Detailed mechanism is not clear.

Page 89: Plasma Assisted Combustion & Chemical Conversion

O3 assisted C2H4 lifted flames -

Two-way phenomenon

42

O3 added after steady lifted flame established, with corresponding uf

Nozzle exit

uf = 3.29 m/s uf = 4.50 m/sO3 addition O3 addition

13% O2 + 87% N2 co-flow

Uco= 0.014 m/s

3500

ppm

0

ppm

0 ppm

2200

ppm

Blow-

out

If flame ascends, blow-out finally happens if O3 too much

Reaction of flame after O3 addition depends on HL,0, both ascend and descend

possible

Effect of ozonolysis reactions

B. Wu, H. Mitchell, W. Sun, T. Ombrello, and C. Carter. “Dynamics of laminar ethylene lifted flame with ozone addition.”

2020 Proceedings of the Combustion Institute, 38, 6773-6780.

Page 90: Plasma Assisted Combustion & Chemical Conversion

CH2O PLIF

43

uf = 3.10 m/s uf = 3.57 m/s

Significant amount of CH2O production owing to ozonolysis

reactions upstream changing flame dynamics

CH2O PLIF

Flame

chemiluminescence

Page 91: Plasma Assisted Combustion & Chemical Conversion

Pri

nce

ton

Un

iver

sity

Combustion lab.

Plasma assisted non-equilibrium chemical synthesis

Page 92: Plasma Assisted Combustion & Chemical Conversion

Pri

nce

ton

Un

iver

sity

Combustion lab.

Plasma assisted chemical reforming: CH4/CO2

400 0C

Ozaki, 22nd ISPC, 2015

Page 93: Plasma Assisted Combustion & Chemical Conversion

Pri

nce

ton

Un

iver

sity

Combustion lab.

Chemical looping?

Catalysis ammonia

Plasma assisted chemical looping: nitrogen fixation

Fig.1 Diagrammatic illustration of nitric acid, hydrogen, ammonia and fertilizer production from air and water through

catalytic plasma nitrogen oxidation and catalyst re-oxidation with water for hydrogen production for ammonia and

fertilizer synthesis.

Page 94: Plasma Assisted Combustion & Chemical Conversion

Pri

nce

ton

Un

iver

sity

Combustion lab.

Annemie Bogaerts, Online Catalysts

Seminar, June 18, 2021

Schneider et al., Nature Catalysis 2018, 1, 269

Plasma assisted chemical reforming: NH3

Plasma catalysis Vibrational excitation

• Which non-equilibrium excitation mode plays a

critical role in ammonia catalysis?

• How much do we understand the mechanism?

Page 95: Plasma Assisted Combustion & Chemical Conversion

Pri

nce

ton

Un

iver

sity

Combustion lab.

Technical questions:

1. Plasma can do a lot of “magics” in combustion

enhancement. Does it really have any “kinetic

merits” on combustion enhancement?

2. How does plasma kinetically enhance ignition, flame

speed, and minimum ignition energy?

3. What are the reaction pathways of plasma assisted

combustion?

4. How does non-equilibrium plasma excitation change

the yield and selectivity in catalysis?

Page 96: Plasma Assisted Combustion & Chemical Conversion

Lecture 3 Plasma assisted combustion: ignition, flame propagation, burning limits, cool flames, and

the minimum ignition energy

Yiguang JuPrinceton University

• Plasma chemistry effect on ignition and ignition limits

• Flame propagation and the effects of heat loss and stretch

• Extinction, quenching distance, and flammability limits

• Ignition assisted flames and cool flames

• The Minimum ignition energy and the critical flame initiation radius

Princeton Combustion Summer School2021.6.21

Page 97: Plasma Assisted Combustion & Chemical Conversion

SL TadFuel/O2 q

Premixed flames

Tad FuelqO2

Diffusion flames

air

Fuel

Ignition, flames and burning limits

2

Auto-ignition: An exothermic, self-accelerating, chain-branching process

Daf=𝑻𝒓𝒂𝒏𝒔𝒑𝒐𝒓𝒕 𝒕𝒊𝒎𝒆𝒔𝒄𝒂𝒍𝒆

𝑹𝒆𝒂𝒄𝒕𝒊𝒐𝒏 𝒕𝒊𝒎𝒆𝒔𝒄𝒂𝒍𝒆 𝒐𝒇 𝒇𝒍𝒂𝒎𝒆

Daf ~ O(1), but Daig → 0 (chemically frozen)

Premixed hot flame

Flam

e t

em

pe

ratu

re, K

Equivalence ratioΦ0L

1200

Lean limit Rich limit

Φ0R

𝑫𝒂𝒇,𝑯 < 𝟏

Chain-branching reaction: H+O2=O+OH

Tem

pe

ratu

re, K

Flame

AB

C D

E

FIgnition

Diffusion hot flames

Stre

tch

exti

nct

ion

Rad

iati

on

exti

nct

ion

Flow residence time

1200

extinction

Flame: An exothermic, luminescent, Diffusion-Ignition Front with chain-branching processes

Page 98: Plasma Assisted Combustion & Chemical Conversion

3.1.1 Ignition and ignition limits

00

/

/

)0(,)0( FF

RTE

FF

RTE

Fp

YYTT

eYBdt

dY

eYBQdt

dTC

P, T0, YF0

0)/( Fp YQTCdt

d

)1(/ 000 qTCQYTT pFad

)1(/)(0

00 qQ

TCQTTCYY

p

pFF

1/

0

0

0

00

0

)(

/

/

/

/

0

RTE

pF

Be

t

RTE

TCQYq

TT

/)1(///// 000 eeeeeRTERTERTERTERTE

Auto-ignition Considering an auto-ignition problem at constant pressure, p, at initial temperature of T0, and fuel mass fraction of YF0.

ρ:densityT: temperatureY: mass fractionQ: heat release per unit mass of fuelE: activation energy

Conservation equation

Adding the mass and energy equations:

0/// 00 QTCYQTCYQTC adpFpFpNormalization:

Page 99: Plasma Assisted Combustion & Chemical Conversion

, oflimit in the : theoryAsymptotic

)/1(1 O

1)0(

)1(1 /)1(

eqd

d

/1

0)0(

qed

d

)1ln( q

growth lexponentia ;/1:imeIgnition t qig

00 /

0

2

01/1

0 )(RTE

F

pRTE

igig eEBQY

TRCBeqt

T

T0

tig

Normalized equation:

a small change in temperature will lead to dramatic change in the reaction rate, therefore, in this limiting case, we have

Solution:

Define: q/1

Plasma effects on homogenous ignition (B, E, T): 1. Increase reaction rate B; 2. Reduce activation energy E, 3. change temperature (heat loss or addition)

Page 100: Plasma Assisted Combustion & Chemical Conversion

00

/

3

0

2/

)0(,)0(

3/4

)(4

FF

RTE

FF

RTE

Fp

YYTT

eYBdt

dY

R

TThReYBQ

dt

dTC

Auto-ignition with heat loss or heat addition Assume: heat addition or loss is a small perturbation O(1/β):

0)0(

Hqed

d

pCR

htH

03

T

T0

tig

h<0

h>0Plasma heat addition/loss will shorten/extend the ignition delay time

Page 101: Plasma Assisted Combustion & Chemical Conversion

Electron impact ionization/dissociation/excitation

e +O2 =O++O+2e (R1a)

e +O2 =O+O(1D) (R1b)

e +O2 =O2(1Δg)+e (R1c)

e +O2 =O2(v)+e (R1d)

Electron ion recombination, attachment, charge transfer

e+O2+ =O+O(1D) (R2a)

O2+ +O2

- =2O2 (R2b)

e+O2 +M = O2- +M (R2c)

H2O+N2+ =H2O

++N2 (R2d)

Dissociation and energy transfer by ions and excited species

N2(A,B,C)+O2 =O+O+N2 (R3a)

O(1D)+H2 = OH+H (R3b)

H+ O2(1Δg)= O+OH (R3c)

N++O2= O++NO (R3d)

CH3+HO2(v)=CH2O+OH (R3e)

N2(v=5) +N2 = N2(v=3) + N2 (R3f)

N2(v) + HO2 → N2 + HO2(v) (R3g)

3.1.2 Plasma chemistry for radical production and gas heating

Recombination/fast heatingRecombination/fast heatingAttachmentCharge Transfer

Radical productionExcitation

Slow heating

>10 eV

~10 eV~1 eV0.2-2 eV

Radical production & fast heating

Page 102: Plasma Assisted Combustion & Chemical Conversion

Pri

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iver

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Combustion lab.

Kinetic ignition enhancement by radical addition

10-7

10-6

10-5

10-4

Mole fraction of radicals added into mixture

10-5

5

10-4

5

Ign

itio

n t

ime

(s)

H2:O2=2:1

T=1000 K

H

O

OH

Chain initiation

Chain-termination

H+O2+(M) → HO2 +(M)

H+OH+(M) → H2O+(M)

H2 +O2 → H+HO2

H2 +O2 → OH+OH

Chain branching and propagation

H+O2 → OH + O

O+H2 → OH + H

OH + H2 → H2O+H

H2O2+M =2OH +M

Slow

Rate limiting

(low P & high T)

Rate limiting

(high P)

Page 103: Plasma Assisted Combustion & Chemical Conversion

Air Air

1

2

5

15

16

3

14

N2

H2 &

N2

7

10

11 12

13

8 6

9

Fuel Fuel 4

N2 N2

1. Silicon Controlled Rectifier, 2. Silicon carbide

heater, 3. R-type thermocouple, 4. Fuel injection

spacer 5. MGA plasma power supply, 5. MGA device,

6. MGA power supply, 7. Cathode, 8. Anode, 9.

Magnets, 10. Gliding arc initiation wire, 11. MGA, 12.

Insulator, 13. Nozzle with N2 co-flow, 14. K-type

thermocouple & FT-IR probe, 15. Diffusion flame, 16.

Water-cooled nozzle with N2 co-flow.

Kinetic effect by NO production on counterflow ignition

Diffusion Flame

Temperature &

Species Measurements

• FTIR, PLIF, Rayleigh

H2/N2

Air/H2/CH4

8

Page 104: Plasma Assisted Combustion & Chemical Conversion

Plasma assisted ignition: H2 Ignition by gliding arc

825

850

875

900

925

950

975

1000

1025

175 200 225 250 275 300 325

Strain Rate, s-1

Ign

itio

n T

em

pera

ture

, K

NP + NF NP + 1% H2NP + 2% H2 P + NFP + 1% H2 P + 2% H2Comp. NP + NF Comp. P + NFComp. P + 2% H2 Comp. NP + 2% H2

NO+HO2=NO2+OH

NO2+H=NO+OH

H+O2+H2O=HO2+H2O

Plasma catalytic effects reduce H2 ignition temperature (Ombrello, T., Ju, Y. and Fridman, A., 2008. AIAA journal, 46(10), pp.2424-2433.)

9

Page 105: Plasma Assisted Combustion & Chemical Conversion

d[H]/dt→infinity

1][

2

2

1 Mk

kNot explosive

1 explosive

H+O2

OH+O (R1)

+(M) HO2 (R2)

HO2+H=OH+OH

H+O2+(M) → HO2 +(M)

H+O2 → OH + O

• Radical and heat production by plasma can extend the explosion limit.

Plasma can break the conventional explosion limit

Page 106: Plasma Assisted Combustion & Chemical Conversion

Pri

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Combustion lab.

Ignition Chemistry: Elementary chain reactions of CH4-O2 system

Chain initiation:

CH4 +O2 → CH3 +HO2

CH4+(M) → CH3 +H+(M)

Chain-branching and propagation

H+O2 → OH + O

CH3 +O2 → CH3O+O

CH3 +O2 → CH2O+OH

CH3 +HO2 → CH3O+OH

CH3O + O2 →CH2O+ HO2

CH3O + M →CH2O+ H+M

CH2O +X →HCO+XH (X=H, OH, O, HO2)

HCO+M→CO+H+M

HCO+O2→HO2+CO

CO+HO2→CO2+OH

Termination reaction

H+O2+M → HO2 +M

CO+OH→CO2+H

Slow

Slow

Opportunity of plasma

Page 107: Plasma Assisted Combustion & Chemical Conversion

12

Kinetics of the ignition: CH4:O2:Ar mixture

(T5=1530 K, n5=5x1018 cm-3)

10-1

100

101

102

103

104

10-6

1x10-5

1x10-4

10-3

10-2

10-1

OH,H,CO2,O

Tem

pera

ture

, K

CH3,H

2O,H

2,CO

CH4

O2

Mo

le f

racti

on

Time, s

1500

2000

2500

Autoignition

10-1

100

101

102

103

104

10-6

1x10-5

1x10-4

10-3

10-2

10-1

Plasma Assisted Ignition

CH2O

H2O

CO2

CO2

H2

CO

H2O

CH3

H

OH

O

CH4

O2

Mo

le f

racti

on

Time, s

1500

2000

2500

Tem

pera

ture

, K

Plasma assisted ignition is characterized by:

– slow increase of gas temperature – developed kinetics of intermediates– partial fuel conversion during induction time

I N Kosarev, N L Aleksandrov, S V Kindysheva, S M Starikovskaia, A Yu Starikovskii, Combustion and Flame, 154 (2008) 569-586

Page 108: Plasma Assisted Combustion & Chemical Conversion

13

Plasma assisted ignition: experiments and

numerical modeling: (CH4-C5H12):O2 + 90% Ar

0.50 0.55 0.60 0.65 0.70 0.75 0.80 0.85

100

101

102

103

104

105

CH4-C

5H

12,

PAI, 0.2-0.7 atm

C2H

6-C

5H

12,

auto, 0.2-0.7 atm

CH4, auto, 0.4-0.7 atm

CH4, auto, 2 atm

Ign

itio

n d

ela

y t

ime, s

1000/T, K-1

Auto Exp, C2H6

Auto Calc, C2H6

PAI Exp, C2H6

PAI Calc, C2H6

, , , C3H8

, , , C4H10

, , , C5H12

I N Kosarev, N L Aleksandrov, S V Kindysheva, S M Starikovskaia, A Yu Starikovskii, Combustion and Flame, 156 (2009) 221-233

Shock tube/nanosecond dsicharge experiments

Page 109: Plasma Assisted Combustion & Chemical Conversion

Plasma kinetic effect on CH4 ignition (gliding arc)

Heated Air (model)

MGA (model)

1000

1050

1100

1150

1200

1250

1300

1350

1400

1450

1500

150 200 250 300 350 400

Strain Rate, s-1

Ign

itio

n T

em

pera

ture

, K

Heated Air (Fotache, Kreutz and Law, 1997)

Heated Air (experiment)

MGA (experiment)

AIAA paper-2007-1025

14Plasma catalytic effects reduce CH4 ignition temperature (Ombrello, T., Ju, Y. and Fridman, A., 2008. AIAA journal, 46(10), pp.2424-2433.)

Page 110: Plasma Assisted Combustion & Chemical Conversion

Residence time

Te

mp

era

ture

Scramjet, afterburner

Plasma generated

species:

O, H, O2(a∆g) …

New “S-curve” by Plasma assisted combustion forsmall molecule fuel such as H2, CH4

the classical S-curve

3.1.3 Plasma Assisted Combustion: The impact of plasma on the ignition and extinction S-curve

The effect of kinetic enhancement (μs ~ ms, 800-1200 K)

Ignition

Extinction

Sun et al. Proc. Comb. Inst. 34, 2010, Combust. Flame 2011, 2012Ombrello et al. 2008

•Strong kinetic enhancement at intermediate temperature•Less effect at high temperature

Plasma

CH4

0.05 0.10 0.15 0.20 0.25 0.30 0.35

1x1015

2x1015

3x1015

4x1015

5x1015

6x1015

7x1015

Smooth

Transition

Extinction

Ignition

O2

=34%

O2

=62%

Fuel mole fraction

OH

nu

mb

er d

en

sity

(cm

-3)

plasma S-curve

Non-thermal plasma dramatically enhances ignition chemistry, but less impact on flame speed/extinction limit!

Page 111: Plasma Assisted Combustion & Chemical Conversion

Nanosecond plasma assisted low temperature ignition of

dimethyl ether ignition in a diffusion counterflow flame

16

0.00 0.02 0.04 0.06 0.08 0.10 0.12

1x105

2x105

3x105

4x105

5x105

6x105

Extinction

increase

decrease

CH

2O

PL

IF (

a.u

.)

Fuel mole fraction

Hot Ignition

P = 72 Torr, a= 250 1/s, f = 24 kHz

XO2=40%, varying Xf

LTC

HTC

S-Curve0.00 0.02 0.04 0.06 0.08 0.10 0.12

1x105

2x105

3x105

4x105

5x105

6x105

increase

decrease

CH

2O

PL

IF (

a.u

.)

Fuel mole fraction

P = 72 Torr, a= 250 1/s, f = 34 kHz,

XO2=60%, varying Xf

New ignition/extinction curve without

extinction limit

LTCHTC

Radical production by plasma can activate LTC at much shorter timescale.

Sun, W., Won, S.H. and Ju, Y., 2014. Combustion and Flame, 161(8), pp.2054-2063.

Page 112: Plasma Assisted Combustion & Chemical Conversion

Plasma activated low temperature combustion pathway

LTC

H+O2=OH+O

Radical production by plasma

Plasma activated high temperature combustion pathway

Plasma activated low temperature

combustion pathway

O+RH → R+OH

R → R’’+2OH

O+RH → R’’+ 3OH

Page 113: Plasma Assisted Combustion & Chemical Conversion

A schematic of the key reaction pathways for high pressure fuel oxidation of at different temperatures

(blue arrow: Below 700 K; yellow arrow: 700-1050 K; red arrow: above 1050 K).

Fuel (RH)

+(OH, HO2)

R

nOH

aldehyde C2H3/CH2O

H/HCO+O2+(M)

+M

+O2

CO2

CO

OQ’O

PlasmaO(1D), O, R, O3

O2(1Δ), N2(v), …

alkene +

+O2

RO2

QOOH

O2QOOH

+O2

KOOH +O2

O2P(OOH)2

H2O2

+O2

HO2

+HO2

Plasma Assisted Combustion Chemistry

• Three chain-branching pathways at low, intermediate, and high temperature• Plasma accelerate low and intermediate chemistry

e +O2=O+O(1D) +e

H+O2(1Δg) =O+OH

O(1D)+RH =OH+R

N2(A,B,C)+O2=O+O+N2

N2(v)+HO2 =OH+O+N2

R(v,*)+O2=RO+OH

=???

O3+M =O+O2+M

Plasma assisted three different flame regimes: cool flame, warm flame, and hot flame

Page 114: Plasma Assisted Combustion & Chemical Conversion

1 2

Hot ignitionLow temperature ignition

0.0 0.1 0.2300

600

900

1200

1500

Tem

pera

ture

(K

)

Time (sec)

R+O2=RO2

HCO+O2=CO+HO2

2HO2=H2O2+O2

H2O2=2OH

H+O2=O+OHO+H2=H+OH

RO2→QOOH →R’+OHO2QOOH →R’’+2OH

Thermal effectKinetic effect

Plasma Activated Low Temperature Combustion for large hydrocarbon fuels

500-800 K

800-1100 K

>1100 K

High

Intermediate

Low

More kinetics effect of PAC at low temperature combustion?

Two-stage ignition: n-heptane

Large molecules Fuel fragments Small molecules

CH2O+X=HCO+XH

Page 115: Plasma Assisted Combustion & Chemical Conversion

τig,Hτig,L

0.01

0.1

1

10

100

0.8 1 1.2 1.4 1.6

Ign

itio

n d

ela

y t

ime

s [

ms

]

1000/T [1/K]

High T ignitionLow T ignitionHigh T ignition (100ppm OH)Low T ignition (100ppm OH)

Stoichiometric n-heptane/air premixture at 20 atm

Constant pressure calculation

1000 K 800 K1250 K

ab

n-heptane HTI

LTI

τig,C~ τf, Daig,C > 0Fast low temperature ignition:

w. 100 ppm OH

Chain-branching reactions

Nu

mb

er

of

oxy

gen

1

2R→RO2→QOOH→O2QOOH→OQ’O +2OH

O2

O2

H2O2→2OH

R’+ HO2→ RO+OH,

O2

H + O2→H+OH

O2

600 KLow Temp.

1200 KHigh Temp.

800 KInt. Temp.

Plasma Activated Low Temperature Combustion for large hydrocarbon fuels

Page 116: Plasma Assisted Combustion & Chemical Conversion

Plasma activated self-sustaining Cool Flames: Radical production

Heated N2 @ 550 K

N2 @ 300 K

Stagnation

plane

Oxidizer @ 300 K

with plasma discharge/

O3

Fuel/N2 @ 550 K

Fig. 1 Schematic of experimental setup

Fig. 2 Plasma and ozone assisted n-heptane cool flames

Cool flame

Hot flame

N-heptane/He

O2/He

Low pressure NSD (60 torr)

(a) Hot diffusion flame

(b) Cool diffusion flame

Tf~1900 K

Tf~650 K

1 atm O3 addition

O3+M=O+O2+M

Sun, W., Won, S.H., Ju, Y. (2014),, Combustion and Flame, 161 (2014) 2054–2063.

Won, S.H., Jiang, B., Diévart, P., Sohn, C.H., Ju, Y., (2015), Proceedings of Combustion Institute, 35, 881-888.

Page 117: Plasma Assisted Combustion & Chemical Conversion

Premixed flames

6/20/2021

Prometheus bringing fire to the earth

History of flame discovery: 3 different stable flames with plasma

1M B.C. 1817

FoodTools

Industrial revolutions

Space Exploration

2000 2010 2012-2013 2015 2017-2018

New enginesNew fuels

Page 118: Plasma Assisted Combustion & Chemical Conversion

Control of low temperature combustion: O3 effects

ELTC

O3 enhanced Extreme LTC of Methyl Hexanoate

Rousso, A.C., Jasper, A.W., Ju, Y. and Hansen, N., 2020. JPC A, 124(48), pp.9897-9914.

23

FuelFig. 1: Ethylene ozonolysis reaction pathway

(primary ozonide, POZ; secondary ozonide: SOZ).

Fuel/O3

Page 119: Plasma Assisted Combustion & Chemical Conversion

10x10-3

8

6

4

2

0

Mo

le F

ract

ion

n-pentane + 500 ppm NO

neat n-pentane

600

500

400

300

200

100

0

Mo

le F

ract

ion

(p

pm

)

NO

NO2

N balance

400

300

200

100

0

Mo

le F

ract

ion

(p

pm

)

775725675625575525

Temperature (K)

HONO

6643.17 cm-1

6642.51 cm-1

6638.26 cm-1

Modeling

• L. Marrodán, Oliver Herbinetet et al., 2019. Chem. Phys. Lett., 719, 22-26.

• Zhao, H. et al., 2018.. C&F 197, 78-87.

RO2 + NO = RO + NO2

NO+HO2<=>OH+NO2

NO2+HO2=HONO+OH

Control of cool flames and warm flames: NOx effect by Plasma

0.1 1500

750

1000

1250

1500

Warm

Hot

Cool

Warm

Ma

xim

um

te

mp

era

ture

Tm

ax [

K]

Strain rate a [s-1

]

0 ppm NO

300 ppm NOTf = 550 K, To = 300 K

Xf = 0.1, Xo = 0.1

P = 8 atm

nC12H26/N2/NO - O2/N2

Cool

100

Cool Flame

Warm Flame

10-1

100

10-1

M. Zhou et al., PCI, vol. 38, 2021

• NO inhibit cool flames• Promote warm flame• Accelerate warm flame reignition

w. NO

N-pentaneSuppressing effect

Enhancing effect

24

0 NOw. NO

50

40

30

20

10

0

ring d

ow

n tim

e (

ms)

6642.86641.86640.86639.86638.86637.8

wave number (cm-1

)

* * **

n-pentane+ NO

HONO(+ NO2 + …)

HONO lines

Page 120: Plasma Assisted Combustion & Chemical Conversion

Flow reactor studies of non-equilibrium plasma-assisted oxidation of n-alkanes

Tsolas, N., Lee, J.G. and Yetter, R.A., 2015. Phil. Trans.

R. Soc. A, 373(2048), p.20140344.

Page 121: Plasma Assisted Combustion & Chemical Conversion

Pri

nce

ton

Un

iver

sity

Combustion lab.

Gundersen et al.

Ignition enhancement by transient corona discharge

Disk electrode & streamers

2-10KV, 20-200ns

•Increased volume

•Transient discharge

Page 122: Plasma Assisted Combustion & Chemical Conversion

Pri

nce

ton

Un

iver

sity

Combustion lab.

Ignition delay time: corona discharge vs. spark

CnHm+e=CnHm-1+H*+e

O2+e=O(1D)+O(3P)+e

Radical production

Large ignition volume?

Liu J, Wang F, Lee L, Ronney P, Gundersen M. In42nd AIAA Aerospace Sciences Meeting and Exhibit 2004 (p. 837).

Page 123: Plasma Assisted Combustion & Chemical Conversion

3.2.1 Adiabatic flame propagation A flame is a self-propagating auto-ignition and thermal diffusion front. The propagation speed of a one-dimensional flame front relative to the far field unburned mixture is the flame speed.

SL

Fuel/airT

Heat conduction

ignition

Reaction zone

YF

0)(,)(

)(,)(

)2(

)1(,

00

2

2

2

2

Fad

FF

FF

p

YTT

YYTT

Wdx

YdD

dx

dYu

qdx

Td

dx

dTuC

Governing equations

RTE

F

F

eYB

QPY

/

2

Enthalpy conservation outside diffusion zone:

q

TC

W

Y

q

TC adpFp

0,0

WC

qYTT

p

F

ad

0,

0

dxWEqqEq

]/)2.(/)1.([

xf

0,0

1

Fad

ad

Y

Y

LeTT

TT

termsconvectionneglect and ]/)2.(/)1.([ dxWEqqEq

fx

x

LeY

Y

RT

E

T

TT

T

TT

F

F

adad

ad

ad

ad

0,

00 ;;

)/1( adTTDefine:

In reaction-diffusion zone:

1st order reaction

Page 124: Plasma Assisted Combustion & Chemical Conversion

D

W

dx

Yd F 2

2

FF dY

D

W

dx

dYd

2][ 2

1)(2)(2

222][

/20,

0

/20,

/0,0,2

adad

ff

F

Ff

RTEFfRTEFf

F

RTE

F

FF

F

Y

Y

F

x

x

eLeY

D

WBdee

LeY

D

WB

deYBLeY

D

Wd

LeY

D

WdY

D

W

dx

dYd

ad

f

RTEFf

xF e

LeY

D

WB

dx

dY /20,2)(2 ][

dxWdx

YdD

dx

dYu F

x

F

x ff

][2

2

fxF

Fdx

dYDuY ][0,

adRTE

p

eC

WBLe

/

2

22 2u)(m

In reaction-diffusion zone (neglect convection):

Rewriting:

Integrating from flame front to a location x in the reaction zone:

Integrating from unburned region to flame front to find the fuel concentration gradient at flame front:

(1)

(2)

Flame speed is affected by Le, B, E, and T. How does plasma affect flame speed?

orderreaction :n,12/ n

adU Mass burning rate:

Page 125: Plasma Assisted Combustion & Chemical Conversion

3.2.2 Flame propagation speed with heat loss or heat addition

0)()(

)(,)(

)2(

)1()(4

00

2

2

4

0

4

2

2

dx

dY

dx

dT

YYTT

Wdx

YdD

dx

dYu

TTKpqdx

Td

dx

dTuC

F

FF

FF

p

tcoefficien absorptionmean :

/

/

/

/

)/()(

0

0

00

PlanckKp

U

xt

U

TCx

Uum

xxX

YYy

TTTT

ad

ref

ref

ad

p

ref

ad

ref

FF

ad

adpadp

ad

UCUC

TKpH

yLe

W

WdX

yd

LedX

dym

HW

dX

d

dX

dm

4

2

2

2

2

2

4

)1(1

)1(exp

2

1

Outer solution (convection diffusion zone):

0X 0

0X )exp(10

mLeXy

0X 1

0X )exp(0

mX

Fuel/air

T

Reaction-diffusion

YF

Convection-diffusion

X=0

Page 126: Plasma Assisted Combustion & Chemical Conversion

dXH

dX

d

dX

dy

LedX

dm

dX

dym ))

1()(

0

00

dXH

dX

d

dX

yd

LedX

dX

dm

dX

dym )

1()(

2

2

2

200

1010 , yyy

m

H

dX

d

dX

dy

Lem

0

11

1)]()0([

2

1100

0

0

ln)0(or 2

)0(exp,0

1m

dX

d

dX

d

dX

dy

Le

m

H

dX

d

m

H

dX

d

m

H

dX

d

dX

dy

Lemm

0

1

00

2 1ln

m

H

dX

d

0

1

Hmm 2ln 22

Adding the mass and energy equation and integrate from upstream boundary to flame front:

Perturbation: assume heat loss or addition only perturb the temperature and mole fraction in O(1/β)

Rewrite the equation above:

Using the jump condition across the reaction zone:

Fuel/air

T

Reaction-diffusion

YF

Convection-diffusion

0- 0+

Find the perturbation in the burned gas zone:

Flame speed with heat loss/addition: How does heat loss/addition affect flame?

Page 127: Plasma Assisted Combustion & Chemical Conversion

Extinction limit and flammability limit:

Hmm 2ln 22

Fig. The dependence of the normalized burning

velocity on the normalized radiative heat loss

of a one-dimensional planar flame.

0.0 0.1 0.2 0.3 0.4 0.50.0

0.2

0.4

0.6

0.8

1.0

Extinction

Limit

e-1

e-1/2

No

rma

lize

d b

urn

ing

ve

loci

ty,

m

Normalized heat loss, HNormalized heat loss 2H

adpadp

ad

UCUC

TKpH

44

adUum /

• For a given mixture with a constant adiabatic flame speed, the increase of heat loss will reduce the flame speed and lead to flame extinction at 2H=1/e and the normalized flame speed at extinction limit is e-1/2

• For a given heat loss intensity (e.g. Kp), as the mixture fuel concentration decreases, the normalized heat loss H will increases. Therefore, at a critical fuel concentration, 2H becomes 1/e, and no flame is available below this fuel concentration. This defines the lean flammability limit.

• How does plasma can change the flammability limit?

Page 128: Plasma Assisted Combustion & Chemical Conversion

Quenching diameter:

Nud

Hf

2

24

releaseheat chemical Total

wall the tolossHeat 2

Nud

mmf

2

2

224

ln

fNued 20

Fuel

Air

wall

wall

Convection Heat losses

Uf

Heat recirculation

For a flame propagating into a tube, the heat loss from the flame to the wall is governed by the convective heat transfer to the wall

0.1 0.2 0.3 0.4 0.5

0.6

0

.7

0.8

0

.9

1

.0

df /20.1 0.2 0.3 0.4 0.5

0.6

0

.7

0.8

0

.9

1

.0

df /2

Fig. Burning rate (solid line) and normalized flamepropagation speed U (U=m in this figure) plotted against

the ratio of flame thickness to channel width (d) for

selected values of reduced heat transfer coefficient (k)

with in a quiescent, two dimensional channel flow.

(Matalon et al. 2003)

Quenching diameter:

Flame speed:

eNu

dH

f 142

2

2

d0: the minimum diameter in which a laminar flame canPropagate.

How does plasma discharge affect the quenching diameter?

Page 129: Plasma Assisted Combustion & Chemical Conversion

3.2.3 Flame speed, extinction and flammability limits with by flame stretch (Le)

0,0

2/

0,2

2

0

2/

0,2

2

)(,)(

0)0(0)0(

)(

)()(

FF

F

f

RTE

FFF

rf

RTE

Fp

YYTT

dx

dY

dx

dT

xxBeYdx

YdD

dx

dYax

TTQxxBeQYdx

Td

dx

dTaxC

ad

ad

u=-ax

Potential flow (outside)ad

ad

ad

RTE

ad

pFad

adpr

T

TT

RT

E

BeU

CQYTT

dxdua

TTKQ

ad

0

2/

0,0

3

0

3

function delta Dirac:

/

/

)(4

adrefref

ad

p

ref

RTE

ad

pFad

ref

FF

ad

Uxt

U

Cx

BeU

CQYTT

xxX

YYy

TT

TT

ad

/

/

/

,/

/

,

2/

0,0

0,

0

0

,2

4 3

Xat

DCLe

UCUC

TKH

ref

p

adpadp

adp

In the limit of large β

0)(21

2

0)(22

2

2/)1(

2

2

2/)1(

2

2

fFF

f

f

f

ead

yd

Led

dy

ea

H

ad

d

d

d

Here the stretch rate a is non-dimensional

dt

dA

Aa

f

f

1Flame stretch:

dxdua /axu

Page 130: Plasma Assisted Combustion & Chemical Conversion

Perturbation

Outer solution in convection-diffusion zone

,.../1...,/...,/111010

FFFF YTplLeYYYTTT

),(at /1,/2222 00

f

tttt dtedteydtedte

ff

),0(at 0,1 00

fy

Jump conditions

0)(2 2/)1(

2

2

ffe

ad

d

(1) Integrating from flame front (-) to end of reaction zone (+)

02 2/1

fead

d

(2) Integrating the summation of mass and energy equation in reaction-diffusion zone,

0

0

d

dyl

d

dp F

02

20

2

02

2

2

H

ad

ydl

d

pd

d

dp F

Governing equation for perturbed variables: and ,0,0 p

Page 131: Plasma Assisted Combustion & Chemical Conversion

Solution: ,2

2/

1

fp

f

eg

a

)/(2

)1

2

1( 11321

2

1

2gIg

a

Hgg

a

H

glp fff

ndeg fn

1 )1(

1

22

1

0

)1(

2

22

dneg fn

dndkk

eeI

f

f

nkn

1

2

)1(1 )1(

11

1222

22

dnn

eg

fn

1

2

)1(

31

122

If ,12, 1

2 gff Hmm 2ln 22

Enthalpy change

am f 2

Page 132: Plasma Assisted Combustion & Chemical Conversion

Flame propagation speed with stretch and heat loss: sublimit combustion

0.1 1 10

0

5

10

15

20

0.1 1 100

5

10

15

20

25

0.1 1 100

5

10

15

20

0.1 1 100.0

0.5

1.0

1.5

2.0

YF=0.0295

X

f

a

YF

=0.0296

X

f

a

YF=0.03

Xf

a

YF=0.029

Xf

a

Dependence of flame location on stretch at Le=0.9

• At low fuel concentration (YF=0.029) below the flammability limit, flame can exist in a narrow range of stretch rate bounded by a radiation extinction limit and a stretched extinction limit.

• As the fuel concentration increase close to the flammability limit, there exist two flame islands, respectively, close and away from the stagnation plane.

• As the fuel concentration further increases to slightly above the flammability limit, there exist both planar flame at zero stretch rate and a near stagnation flame island at Lewis number below unity.

• As the equivalence ratio becomes above flammability limit, the two flame islands merge together and a stretched flame can becomes a planar flame as the stretch rate decreases.

Le=0.9

Ju, Y. and Minaev, S., 2002. Proceedings of the Combustion Institute, 29(1), pp.949-956.

Page 133: Plasma Assisted Combustion & Chemical Conversion

Microgravity experiments

Maruta, K., Yoshida, M., Ju, Y. and Niioka, T., 1996, Symposium

(International) on Combustion (Vol. 26, No. 1, pp. 1283-1289). Elsevier.

Page 134: Plasma Assisted Combustion & Chemical Conversion

0 10 20 30 40

1200

1250

1300

1350

1400

1450

m

l

T0=1358.

0.46

k.

j

i

h..

..

...

.

. .

0.450.46

0.469

0.469 =0.48

g

fed

cb

a

Le=1.4

Fla

me

tem

per

ature

(K

)

Stretch rate (s-1)

x

T

NFDF NSF WF

Numerical simulation: detailed chemistryCH4-O2-N2-He

Page 135: Plasma Assisted Combustion & Chemical Conversion

Stan

dar

dlim

it

Temperature curve of 1D planar propagating flame

B

CE(FSWSF limit)

DF

Stretched flame

AG

WF

Stretch rate, a

0

0'

G-curve(Le < Lecr)

Limit of NSF

The G-Curve

Page 136: Plasma Assisted Combustion & Chemical Conversion

0.4 0.6 0.8 1

Equivalence ratio

10-1

100

101

102

103

Str

etc

h r

ate

at

exti

ncti

on

(1/s

)

Le=0.967

F

B

C

D

E

Stretch limit of normal flame

CH4/AIR A

Radiation limit of weak flame

Jump limit of weak flame

Radiation limit

of NSF

0.488

,

F

G

experiment

The G-curve (Le < Lecr )

Ju, Y., Guo, H., Maruta, K. and Liu, F., 1997..JFM, 342, pp.315-334.Guo, H., Ju, Y. and Niioka, T., 2000. CTM, 4(4), pp.459-475.

Φ0

Φ0

When a mixture has a low Lewis number, the flammability (Φ0) region can be extended significantly by stretch!

Page 137: Plasma Assisted Combustion & Chemical Conversion

0.4 0.6 0.8 1

Equivalence ratio

10-1

100

101

102

103

Str

etc

h r

ate

at

exti

nct

ion

lim

it (

1/s

)

C3H8/Air

Standard limit

A

B

E

C

D

F

G

, Experiment

The K-curve (Le > Lecr )Now we can understand the experimental data on the figure below

How does plasma change the flammable region of stretched flames?

Page 138: Plasma Assisted Combustion & Chemical Conversion

3.3.1 Plasma enhancement and flame speed Gliding arc on flame extinction experiment

Diffusion Flame

H2/N2

Air/H2/CH4

0

50

100

150

200

250

300

350

19 20 21 22 23 24 25 26

Percent Methane Diluted in Nitrogen

Str

ain

Rat

e, 1

/s

Bundy et al.

Puri & Seshadri

No Plasma

33 Watts44 Watts

60 Watts

78 Watts

78W

60W

44W

33W

0W

0.00E+00

6.00E+15

1.20E+16

1.80E+16

-0.4 -0.2 0 0.2 0.4

Distance Between Nozzles, cm

Nu

mb

er

De

nis

ty o

f O

H

0 Watts, a=83.3 1/s

48 Watts, a=183 1/s

78 Watts, a=127.7 1/s

Computation

0 W 48 W 78 W

Role of plasma: mainly thermal effect

Ombrello, T., Qin, X., Ju, Y., Gutsol, A., Fridman, A. and Carter, C., 2006. AIAA journal, 44(1), pp.142-150.

Page 139: Plasma Assisted Combustion & Chemical Conversion

Pressure

Sp

ecie

s L

ifet

ime

1 atm

ramjets &

scramjetsgas turbinesICE’s PDE’s

Plasma Generated Active Species

Lifetime vs. Pressure

long lifetime

10-1000 times

more reactive

than O2

What are the effects of O3, O2(a1Δg), O, … on flame propagation?

O2(a1Δg)

Page 140: Plasma Assisted Combustion & Chemical Conversion

Enhancement of flame Speed by plasma generated O3

u

bliftedL SS

10 mm

0.2

0.3

0.4

0.5

0 0.005 0.01 0.015

Mixture fraction gradient dY F /dR

Sli

fted

[m

/s]

0

2

4

6

8

10

12

14

En

ha

nce

men

t [%

]

0 ppm O3 592 ppm O3

1110 ppm O3 1299 ppm O3

1299 ppm O3

1110 ppm O3

592 ppm O3

(~ 1/axial distance)

Flame speed extraction

Nozzle Tip

Lifted C3H8/O2/N2 flames

Ombrello, T., Won, S.H., Ju, Y. and Williams, S., 2010. Part I:

Effects of O 3. Combustion and flame, 157(10), pp.1906-1915.

Page 141: Plasma Assisted Combustion & Chemical Conversion

Kinetic Thermal Enhancement Mechanism by O3

0

2

4

6

8

10

12

14

0 1000 2000

Fla

me S

peed

En

ha

ncem

en

t [%

]

Concentration of O3 [ppm]

SL (O3 decomposing in pre-heat zone)

SL (O3 to O2 far upstream of pre-heat zone)

Extrapolated Enhancement (experiment)

O3

O2

O

C3H8

C3H7+OH

O3

Fla

me

Pre

-He

at Z

on

e

Reactants

Products+H2O

+HEAT

or other stable

species

O3+O3 O2+O2+O2

Kinetic, Curvature and Stretch Effects

Radical production by plasma mainly accelerates heat release (not change branching).

Kinetic-thermal effect!

Page 142: Plasma Assisted Combustion & Chemical Conversion

Kinetic Effect by O2(a1Δg) on flame propagation

O2 (a1Δg) at 0.98 eV

O2 (b1Σg+) at 1.6 eV

O2 (a1Δg) + H = OH+O fast

O2 + H = OH +O slow

Page 143: Plasma Assisted Combustion & Chemical Conversion

Lifted flame experimental system

microwave

power supply

T3

T2 T1 fuel

oxidizer

φ=1camera

O2

Ar

ignition

system

P1

P2

Lifted Flame

NO

ICOS Cavity

FTIR

C3H8 or C2H4

O3

Absorption

Cell

vacuum

pump

3-way

valve

vacuum

pumpIn

ten

sity

254 nmWavelength

w/o O3

w/ O3

Hg light

emissionlower light

intensity

254nm

Detector

Notch

Filter

Flow

Hg Light

O3

O3

O3

O3

O3

O3

O3

O3 O

3

Off-Axis ICOS Cavity

Diode LaserComputer

PD

LensMirror

LensMirror

Flow Flow

NOx

O3

O2(a1Δg)

6636.16 6636.20 6636.24

Frequency [cm-1]

Cro

ss-Sectio

n

(x1

0-2

3) [cm

2]

Ca

vit

y E

nh

an

ced

Ab

sorp

tio

n (

GA

)

Q(12) Experimental measurement

Q(12) Curve fit

Page 144: Plasma Assisted Combustion & Chemical Conversion

O2(a1Δg) Enhancement of C2H4 Flame Speed

[O2(a1Δg)], ppm ΔHL, mm

3137 4.76

4470 6.82

4627 6.83

5098 7.31

0

1000

2000

3000

4000

5000

6000

4 5 6 7 8

Change of Flame Liftoff Height, ΔHL [cm]

Con

cen

trati

on

[p

pm

]

SDO (w/ NO)

SDO (w/o NO)

O3 (w/o NO)

Energy Coupling Into Flow

≈ 1 eV to produce O2(a1Δg)

≈ 5000 ppm O2(a1Δg) 2-3 % Lifted Flame Speed Enhancement

Microwave Power = 80 Watts

Nozzle Tip

O2 (a1Δg) + H = OH+O fast

O2 + H = OH +O slow

Hydrocarbon quenching?

Far less than

Ombrello, T., Won, S.H., Ju, Y. and Williams, S., 2010.

Part II: Effects of O 2 (a 1 Δ g). Combustion and

Flame, 157(10), pp.1916-1928.

The kinetic effect of O3 and O2(a1Δg)

on flame speeds is small.

Page 145: Plasma Assisted Combustion & Chemical Conversion

Effect of O production in nanosec plasma on

flame extinction

50-20 -15 -10 -5 0 5 10 15 20

-2000

0

2000

4000

6000

8000

Vo

lta

ge

(V)

Time (ns)

FWHM= 6 ns

f = 5~50 kHz

20 & 28 mm ID

15.24 mm × 22 mm

10 mm

E/N~10-15 Vcm2

10 mm away from exit

Power~0.7 mJ

f=40 kHz

Page 146: Plasma Assisted Combustion & Chemical Conversion

Atomic O measurement (TALIF) and effect of extinction limit

51

Ar diluted CH4/O2 diffusion flame:

XO2=0.28, Peak voltage= 7 kV, P= 60 Torr

0.30 0.31 0.32 0.33 0.34 0.35 0.36

150

225

300

375

450

525

computation (T=348 K)

computation (T=398 K)

computation (T=528 K)

computation (T=528 K)

2000 ppm O addition

Fuel mole fraction XfE

xti

nct

ion

str

ain

ra

te (

1/s

)

no plasma

with plasma (f=5 kHz)

with plasma (f=20 kHz)

heated flow (T=398 K)

heated flow (T=528 K)

0 5 10 15 20 25 30 35 40 45

0

2

4

6

8

10

12

14

Ato

mic

ox

yg

en c

on

cen

tra

tio

n (

10

15

cm

-3)

Pulse repetition frequency (kHz)

Sun, W., Uddi, M., Ombrello, T., Won, S.H., Carter, C. and Ju, Y.,

2011. Proceedings of the Combustion Institute, 33(2), pp.3211-3218.

“O production has minor kinetic effect on flame extinction!”

Page 147: Plasma Assisted Combustion & Chemical Conversion

Flame speeds vs. O3 addition: Steady C2H4 lifted flames

with - Two-way phenomenon

52

O3 added after steady lifted flame established, with corresponding uf

Nozzle exit

uf = 3.29 m/s uf = 4.50 m/sO3 addition O3 addition

13% O2 + 87% N2 co-flow

Uco= 0.014 m/s

3500

ppm

0

ppm

0 ppm

2200

ppm

Blow-

out

If flame ascends, blow-out finally happens if O3 too much

Reaction of flame after O3 addition depends on HL,0, both ascend and descend

possible

Effect of ozonolysis reactions B. Wu, H. Mitchell, W. Sun, T. Ombrello, and C. Carter. 2020 Proceedings of the

Combustion Institute, 38, 6773-6780.

Page 148: Plasma Assisted Combustion & Chemical Conversion

CH2O PLIF

53

uf = 3.10 m/s uf = 3.57 m/s

Significant amount of CH2O production owing to ozonolysis

reactions upstream changing flame dynamics

CH2O PLIF

Flame

chemiluminescence

Page 149: Plasma Assisted Combustion & Chemical Conversion

54

SL=SL(Daig) ?

x

T

T0

Tp

Ti

Tf

𝑺𝑳~𝑺𝑳,𝑫𝒂,𝒊𝒈=𝟎 ∗𝑻𝒇 − 𝑻𝟎

𝑻𝒊 − 𝑻𝒑

𝑻𝒑 =𝑻𝒂

𝐥𝐧[ 𝟏 − 𝑫𝒂, 𝒊𝒈

𝒆𝑻𝒂𝑻𝟎 +𝑫𝒂

, 𝒊𝒈𝒆𝑻𝒂𝑻𝒇]

𝑫𝒂𝒊𝒈 =𝝉𝒇

𝝉𝒊𝒈 𝑻𝟎, 𝑷, 𝝓

𝝎 = 𝑨𝑻𝒃 𝐞𝐱𝐩 −𝑻𝒂𝑻

Ignition Flame

𝑇𝑎 → ∞, 𝑻𝒊→ 𝑻𝒇

b=2

Zhang, T. and Ju, Y., 2020. C&F, 211, pp.8-17.

Cool flame speed, SL, exponentially increases with Daig

Flames in cavityRCCI

Convection-diffusion-reaction front

3.3.2 Ignition assisted flame propagation: the role of plasma in enhancing flame speed

Page 150: Plasma Assisted Combustion & Chemical Conversion

3.4 Plasma effect on the minimum ignition energy and the critical flame initiation radius

Lefkowitz et al. 2012, Ikeda et al. 2009

Internal combustion engine, microwave

Flammability limit?

Spark Microwave gliding arc Multi sparks

Why does a flammable mixture can not be ignited by a spark for a small engine or at lower pressure?

Page 151: Plasma Assisted Combustion & Chemical Conversion

Puzzle of high altitude relight: an unresolved ignition problem or a flame problem?

Altitude

[1/p]

Flight speed

Flow speed

Is the flame speed really a problem for relight?

Flame speed ~ pn/2-1

Engineinstability Flow

speed

Page 152: Plasma Assisted Combustion & Chemical Conversion

Q ?

• What governs the ignition & Eig?

• What are the chemistry and

transport effects?

•Eig,min: Defined by stable “flame ball” size?Zeldovich et al. (1985), Champion et al. (1986)

LeTTCRE adpZig ~)(3

4 3

Larger fuel molecules larger Eig

•Eig,min: Defined by flame thickness, δ (make a guess)?

B. Lewis and Von Elbe (1961), Ronney, 2004, Glassman (2008)

11

)(3

42/33

3

LeSTTCE

u

adpig

Larger fuel molecules smaller Eig

volume heat capacity

Ignition sparkto a flame

δ

fuelJet

oxygenLe

ydiffusivit Mass

ydiffusivit Thermal

Page 153: Plasma Assisted Combustion & Chemical Conversion

Temperature

Fuel concentration

T ~ 1/r

Reaction zone

Interior filled with combustion

products

Fuel & oxygen diffuse inward

Heat & products

diffuse outward

C ~ 1-1/r

T*

T•Q

Assumptions and simplification: • 1D quasi-steady state, Constant properties• One-step chemistry• Center energy deposition

H

r

Tr

rrr

TU

t

T)(

1 2

2

)( 2

2

1

r

Yr

rr

Le

r

YU

t

Y

)~~

(~~~

~~

0

0

TTSC

HH

aduP

f

)()1(

1

2exp Rr

T

TZ

f

f

0,/,0 2 YQrTrr

0,, YTTRr f

1,0, YTr

00 ~

~

,~

~

f

f

f

rR

rr

f

f

R

ULeULeR

QfT

TZdeeR

LeQT

)1(

1

2exp/

1 22

Flame speed: effect of flame radius, heat addition and Lewis number

Chen, Z. and Ju, Y., 2007. Combustion Theory and Modelling,11(3), pp.427-453.

Le: Lewis numberZ: activation energyσ: density ratioU: flame speedQ: ignition energyΩ: analytic functions

Page 154: Plasma Assisted Combustion & Chemical Conversion

Flame Radius, R

Fla

me

Pro

pa

ga

tin

gS

pe

ed

,U

10-2

10-1

100

101

102

10-3

10-2

10-1

100

101

Q=0.00

Q=0.05

Q=0.092

Q=0.10

Q=0.20

a

bc

d

e

f

g

h

i (a), Le=1.0, h=0.0

Flame Radius, R

Fla

me

Pro

pa

ga

tin

gS

pe

ed

,U

10-1

100

101

102

10-2

10-1

100

101

Q=0.0

Q=0.1

Q=0.15

Q=0.6

(a), Le=1.2, h=0.0

a

b

cd

e

f

g

h

i

j

Flame radius, R

Fla

me

pro

pa

ga

tin

gsp

ee

d,U

10-1

100

101

102

0.0

0.4

0.8

1.2

1.6

Le=0.5

0.8

1.01.2

2.0

OO O O O

adiabatic(h=0.0)

O

1.4U=0:

Flame

ball

Extinction

limit

1. The critical ignition size and energy is governed by two different length scales:

•Flame ball size (small Le)•Extinction diameter (large Le)

Chen & Ju, Comb. Theo. Modeling, 2007

2. With ignition energy, there is a critical flameinitiation radius, below which, ignition will fail eventhe mixture is above the flammability limit.

Q ?

The Critical Ignition Radius

Page 155: Plasma Assisted Combustion & Chemical Conversion

60

Ignition by heat and radical deposition

LeF = 2.2

R

U

10-1

100

101

102

10-3

10-2

10-1

100 Le

Z= 1.0

LeF

= 1.0

qt

= 0.0

12

3

4

5

1: qc

= 0.0

2: qc

= 0.4

3: qc

= 0.8

4: qc

= 1.0

5: qc

= 1.2

R

U

0 0.05 0.1 0.15 0.20

0.05

0.1

4

5

3

Radical Only

R

U

10-1

100

101

102

10-3

10-2

10-1

100

LeF

= 2.2

LeZ

= 1.0

qt

= 0.05

1: qc

= 0.0

1

(b)

R

U

10-1

100

101

102

10-3

10-2

10-1

100

LeF

= 2.2

LeZ

= 1.0

qt

= 0.05

1: qc

= 0.0

2: qc

= 0.5

2

21

(b)

R

U

10-1

100

101

102

10-3

10-2

10-1

100

LeF

= 2.2

LeZ

= 1.0

qt

= 0.05

1: qc

= 0.0

2: qc

= 0.5

3: qc

= 0.675

2

2

3

3

3

1

(b)

R

U

10-1

100

101

102

10-3

10-2

10-1

100

LeF

= 2.2

LeZ

= 1.0

qt

= 0.05

1: qc

= 0.0

2: qc

= 0.5

3: qc

= 0.675

4: qc

= 0.7

2

2

3

4

3

3

44

1

(b)

1st

flame

bifurcation

R

U

10-1

100

101

102

10-3

10-2

10-1

100

LeF

= 2.2

LeZ

= 1.0

qt

= 0.05

1: qc

= 0.0

2: qc

= 0.5

3: qc

= 0.675

4: qc

= 0.7

5: qc

= 0.73

2

2

3

4

3

3

44

5

5

1

(b)

2nd

flame

bifurcation

R

U

10-1

100

101

102

10-3

10-2

10-1

100

LeF

= 2.2

LeZ

= 1.0

qt

= 0.05

1: qc

= 0.0

2: qc

= 0.5

3: qc

= 0.675

4: qc

= 0.7

5: qc

= 0.73

6: qc

= 1.0

2

2

3

4

3

3

6

44

5

5

6

1

(b)

Chen et al. 2011

Critical flame initiation radius

• Outwardly propagating flames• n-Decane/Air at ϕ 0.7, 1 atm, 400 K• Schlieren imaging 15000 fps

60

1 cm

0 2 4 6 8 10 12 14 16 18

0.0

0.5

1.0

1.5

2.0

2.5

Time [ms]

Fla

me

ra

diu

s R

f [c

m]

60

80

100

120

140

160

180

Fla

me

sp

ee

ds

dR

f / d

t [c

m/s

]

Flame radius

Flame speed

Won, Santer, Dryer, Ju, 2012

Page 156: Plasma Assisted Combustion & Chemical Conversion

Cube of critical flame radius, RC

3

Min

imu

nig

nitio

np

ow

er,

Qm

in

0 500 1000 1500 2000 25000

0.5

1

1.5

2

Z = 10

Cube of critical flame radius, RC

3

Min

imu

nig

nitio

np

ow

er,

Qm

in

0 500 1000 1500 2000 25000

0.5

1

1.5

2

Z = 13

2.0

1.4

1.6

1.7

1.8 = Le

1.9

1.51.4

2.5

2.0

1.9

1.8

1.7

1.6

1.5

Le = 2.1

2.3

2.4

2.2

Minimum Ignition Energy vs. Critical ignition radius:

impacts of flame chemistry and transport

Chen, Burke, Ju, Proc. Comb. Inst. Vol.33, 2010

Activation energy

0

0.5

1

1.5

2

2.5

3

0.6 0.7 0.8 0.9 1

Cri

tic

al r

ad

ius

[c

m]

Equivalence ratio

JP8 POSF 6169

SHELL SPK POSF 5729

@ 1 atm

Unburned Temperature = 450 KFuel/Air (21% O2) mixture

Fuel Mean molecular

weight

Radical Index

JP8 POSF 6169 153.9 0.80

SHELL SPK POSF 5729

136.7 0.85

Won, Santer, Dryer, Ju, 2012

Page 157: Plasma Assisted Combustion & Chemical Conversion

What controls ignition in engine? Critical Ignition Radius

Theory: Ignition to flame transition(critical ignition radius, Rc)

Flame Radius, R

Fla

me

Pro

pa

ga

tin

gS

pe

ed

,U

10-1

100

101

102

10-2

10-1

100

101

Q=0.0

Q=0.1

Q=0.15

Q=0.6

(a), Le=1.2, h=0.0

a

b

cd

e

f

g

h

i

j

Critical ignition radius

Rc

Q

?

0

0.5

1

1.5

2

2.5

3

0.6 0.7 0.8 0.9 1

Cri

tic

al r

ad

ius

[c

m]

Equivalence ratio

JP8 POSF 6169

SHELL SPK POSF 5729

@ 1 atm

Unburned Temperature = 450 KFuel/Air (21% O2) mixture

• Spark size > Rc, but…• Rc increases with leaner mixtures• Rc increases with EGR• Rc increases with smaller engines

How to successfully ignited lean mixtures?

Solution? Turbulent jet or volumetric ignition?

How big is the critical ignition radius?

1.5-2.5 cm at 1atm

t=0.5ms t=28.5msSingle spark

3 cascading sparks at the same total energyCH4/air

Z. Chen and Y. Ju, CST, 2007

H Zhao et al., CNF, 2019

Advanced engine

Page 158: Plasma Assisted Combustion & Chemical Conversion

63

Subsonic Ignition Tunnel Utilized

to Elucidate Fundamental Interactions

• Subsonic Wind Tunnel ◦ Premixed methane/air at room temperature and pressure

◦ U = 1 - 10 m/s

◦ Re = 6,000 - 24,000

◦ Optical access through windows on three sides

•Transient Plasma Systems Pulsed Power Supply ◦ 10 ns FWHM

◦ Pulse repetition frequency (PRF) up to 330 kHz

◦ Peak voltage of 10 kV into 50 Ω resistor

◦ Maximum Energy Per Pulse ≈3 mJ

•Electrodes◦ Lanthanated tungsten

◦ Pin-to-pin configuration

◦ Micrometer controlled inter-electrode gap distance

◦ Tip angle of 20° Courtesy of Timothy Ombrello

Page 159: Plasma Assisted Combustion & Chemical Conversion

64

300 kHz 100 kHz 20 kHz 10 kHz 5 kHz 2 kHz 1 kHz3.3 kHz 2.5 kHz

Fully-Coupled Partially-Coupled Decoupled

Effect of Time Scale of Energy DepositionFixed Total Energy and Varying Pulse Repetition Frequency (PRF)

3.3 µs 10 µs 50 µs 100 µs 200 µs 500 µs 1000 µs300 µs 400 µs

CH4-Air, φ = 0.6, U = 10 m/s, D = 2 mm, and N = 20

Three Distinct Regimes Identified

Page 160: Plasma Assisted Combustion & Chemical Conversion

J.K. Lefkowitz, T. Ombrello / Combustion and Flame 180 (2017) 136–147

Larger ignition size, leaner mixture ignition

Effect of ignition kernel size on ignition probability

Page 161: Plasma Assisted Combustion & Chemical Conversion

66

• Increasing power deposition rate (high PRF) is a superior method to ensure ignition

• In partially-coupled regime, more pulses increases ignition probability, but not to 100%

• In decoupled regime, ignition probability is a linear function of number of pulses

MIP = Minimum Ignition Power (determined for 50% ignition probability)

Fully-Coupled Partially-Coupled

De-

coupled

Effect of Inter-Pulse Time

and Number of Pulses

0

10

20

30

40

0 5 10 15 20

MIP

(W

)

Number of Pulses

CH4-Air, φ = 0.6, U = 10 m/s, D = 2 mm, and N = 20

Ignition probability is dependent on PRF (inter-pulse time), not total energy deposition!

Page 162: Plasma Assisted Combustion & Chemical Conversion

Overlaid Schlieren and High Speed OH-PLIF Diagnostics

February 27th, 2021 Combustion Webinar 67

Flow𝑼 = 10 m/s• Schlieren images (grey-scale) show warm gas

• OH-PLIF images show burned gas

• Higher PRF Schlieren and OH-PLIF largely overlap

Larger OH region

Greater intensity of OH-PLIF signal

• Lower PRF Schlieren and OH-PLIF differ drastically

More likely to be quenched

PRF (kHz) = 2 5 10 25 50 100 200

Scale × 2

J. Lefkowitz, Combustion Webinar, Lecture 28, 2021. https://youtu.be/ckIOU4PnyTA

Page 163: Plasma Assisted Combustion & Chemical Conversion

68

How Does This Translate to a More Realistic FlowImplications in a Recirculating Turbulent

Reactive Flow: Mach 2 Cavity

NP

HF

D (

300 k

Hz)

Cap

acit

ive D

isch

arg

e

M=21.65 cm

22.5°

6.6 cm

2.54 cm

1.9 cm

Steady-State

Chemiluminescence

Time to Ignition

for NPHFD

Time to Ignition for

Capacitive Discharge

Page 164: Plasma Assisted Combustion & Chemical Conversion

69

Time to Ignition for Lean Cavity (~Φ=0.8)Energy Deposition of 50-800 mJ

Drastic Change in Ignition

Time Below ~ 100 mJ

Approximately 1

Cavity Cycle Time

Factor of 7 Difference in Energy

Deposition, But Same Ignition Time

Directly Ties to The Subsonic

Benchtop Experiments to Highlight

Synergy Between Pulses and the

Effect on Flame Growth Rates

Page 165: Plasma Assisted Combustion & Chemical Conversion

70

Bluff-body stabilised premixed flames (Dawson et al, Proc Comb Inst 33:1559-1566, 2011)

same, U increases

OPEN

ENCLOSED<OH*>

Prior to BO

E. Mastorakos

Page 166: Plasma Assisted Combustion & Chemical Conversion

71

Build-up of CH2O in the RZ close to LBO

Kariuki et al, PROCI 35

Simultaneous CH2O – OH PLIF

Inst

Mean

Close to LBO

Close to LBOFar from LBO

E. Mastorakos

OH+CH2O=HCO+H2O

O(L/U) ~ O(α/SL2)

Plasma assisted flame stabilization

Page 167: Plasma Assisted Combustion & Chemical Conversion

72

(c)

Ignition assisted turbulent flame propagation SL=SL(Daig)

• N-heptane/air

• OH PLIF 10 kHz, 40 ms duration

Reactor-assisted turbulent slot (RATS) burner

B. Windom et al., C&F 169, 2016, pp.19-29

Page 168: Plasma Assisted Combustion & Chemical Conversion

Summary: The impact of plasma on fundamental combustion properties:

How does plasma assist combustion? Ignition, Flame speed/limit, Emin

Ignition/extinction S-curveFlame speed and propagation

(Flammability limit)

High temperature flame

Flam

e t

em

pe

ratu

re, K

Equivalence ratioΦ0

1200

Φ0,r

Flow residence time

Te

mp

era

ture

, K

Ignition

Extinction

1500

Ignition to flame transition(critical radius, Rc)

Flame Radius, R

Fla

me

Pro

pa

ga

ting

Sp

ee

d,U

10-1

100

101

102

10-2

10-1

100

101

Q=0.0

Q=0.1

Q=0.15

Q=0.6

(a), Le=1.2, h=0.0

a

b

cd

e

f

g

h

i

j

Critical ignition radius

Rc

Q?

• Shorten ignition time• Extend extinction limit

Plasma

Plasma

• Increase flame speed• Extend flammability limit

• Make ignition kernel > Rc• Accelerate ignition to flame transition

0/

0

2

0 RTE

F

p

ig eEBQY

TRCt adRTE

p

L eC

WBLeS

/

22

Ignition delay Mass burning rate

3

0min )( cadp RTTCE

Minimum ignition energy

Page 169: Plasma Assisted Combustion & Chemical Conversion

Summary

1. Plasma has both kinetic and thermal effects on ignition enhancement.

2. Plasma has only minor kinetic effect on flame propagation speed at high temperature. The main effect for the extension of extinction limit is thermal. However, plasma can enhance ignition assisted flame speed significantly.

3. Plasma may have strong kinetic effect on cool flame and warm flame propagation speed and limits.

4. Plasma can cause fuel fragmentation and reduce the fuel Lewis number, thus enhance flame speed via the Lewis number effect (Transport).

5. The minimum ignition energy is governed by a Critical Radius. Plasma can create a large volumetric discharge greater than the critical radius to reduce the minimum ignition energy, especially at low pressure and fuel lean conditions.