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Developing Secondary Organic Aerosol (SOA) Code for the MCM David Johnson (Mike Jenkin and Steve Utembe) Department of Environmental Science and Technology, Imperial College London, Silwood Park, Ascot, SL5 7PY MCM Developer and User Workshop, Leeds, Thursday/Friday 2/3 December 2004

Developing Secondary Organic Aerosol (SOA) Code for the MCM David Johnson (Mike Jenkin and Steve Utembe) Department of Environmental Science and Technology,

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Developing Secondary OrganicAerosol (SOA) Code

for the MCM

David Johnson

(Mike Jenkin and Steve Utembe)

Department of Environmental Science and Technology, Imperial College London, Silwood Park, Ascot, SL5 7PY

MCM Developer and User Workshop, Leeds,

Thursday/Friday 2/3 December 2004

Introduction

Effects of particulate matter in the atmosphere

Contribution that organic material makes to total particulate burden

SOA from atmospheric oxidation of biogenic volatile organic compounds (VOCs) and anthropogenic aromatic hydrocarbons

Gas-phase degradation mechanisms

Transfer of material from gas- to condensed organic-phase

Formation of SOA and Oxidation Mechanisms

VOC higher polarity, lower volatility products SOA material

Generally only for VOC ≥ C6

aromatic hydrocarbons (e.g. toluene, ethylbenzene, xylenes)terpenic biogenic hydrocarbons (e.g. -pinene, -pinene)

Oxidation mechanisms for large VOCs are very complex

Master Chemical Mechanism (MCM)

e.g. for toluene (methylbenzene) : 268 species, 754 reactions

ca. 120 species with Tb > 450 K

Gas-to-particle partitioning of organic material

Pankow absorption model

Transfer of material represented as a dynamic equilibrium

POH (g) POH (abs)

[POH(abs)]/[POH(g)]

= kin[POH(g)] / kout MO

= Kp MO

Lp

RTK

om

9

p

MW

10501.7

Odum et al. “two-product”-model

0

0.5

1

1.5

2

2.5

3

3.5

4

4.5

5

0 100 200 300 400

aerosol concentration (M 0) / g m-3

ae

roso

l yie

ld (Y

) / %

i = 1,2

i

iYY

i p

pi

MK

MK

0

0

1

At small M0

Y M0 Kp,i

As M0 Y i

MCM v3.1-“many product”-model

Pankow absorption model

e.g. for toluene, ca. 150 species with Tb > 450 K

Transfer of material represented as a dynamic equilibrium

POH (g) POH (abs)

[POH(abs)]/[POH(g)]

= kin[POH(g)] / kout[OA]

= Kp [OA]

Lp

RTK

om

9

p

MW

10501.7

need to estimate saturated vapour pressures for 150 species

T

T

T

T

R

TSp bbbvapln8.018.1

)(

760ln

L

How to estimate Kp,i for a large number of species?

Use the MCM (Accord) Database and ChemDraw for Excel

1. Convert to unique SMILES strings.

How to estimate Kp for a large number of species?

Use the MCM (Accord) Database and ChemDraw for Excel

2. “Eliminate” radical species (replace “[O]” with “Z”)

How to estimate Kp for a large number of species?

Use the MCM (Accord) Database and ChemDraw for Excel

3. Sub-structure search for oxynitro-compounds (organic nitrates)

Use the MCM (Accord) Database and ChemDraw for Excel

4. Molecular property calculations using Chem Office for Excel

How to estimate Kp for a large number of species?

Use the MCM (Accord) Database and ChemDraw for Excel

4. Molecular property calculations using Chem Office for Excel

How to estimate Kp for a large number of species?

“Deployment” of Kp values

“on-line” vs. “off-line”

kin = 6.2 10-3 s-1

kout = kin / Kp

Average MW ofAbsorbing organic condensed-phasespecies

Smog Chamber Aerosol Data

e.g. for toluene data from EXACT (Effects of the oXidation of Aromatic Compounds in the Troposphere)

0

10

20

30

40

50

60

9 11 13 15 17

hour

ae

roso

l ma

ss / g

m-3

0

150

300

450

[tolu

en

e, 2

x NO

, 2 x N

O2 ] / pp

bv

All partitioning coefficients

27.5

Condensed-Phase Chemistry (Association Reactions)

R R'

OH

+ R"OOH R

OH

R'

OOR

peroxyhemiacetal

Tobias and Ziemann

0

5

10

15

20

25

30

35

40

9 10 11 12 13 14 15hour

Simplified Peroxyhemiacetal Chemistry

ROOH + HC(=O)R’ ROOC(OH)R’H

adduct forming chemistry included

Simplified Peroxyhemiacetal Chemistry

ROOH + HC(=O)R’ ROOC(OH)R’H

0

5

10

15

20

25

30

35

40

9 10 11 12 13 14 15

hour

27.5 (original model)

9.9 (association chemistry)

Effect of NOx on Toluene SOA

0

10

20

30

40

50

60

9 11 13 15 17

hour

ae

roso

l ma

ss / g

m-3

0

150

300

450

[tolu

en

e, 2

x NO

, 2 x N

O2 ] / pp

bv

Effect of NOx on Benzene SOA

0

10

20

30

40

50

60

9 10 11 12 13 14 15 16 17

hour

aero

sol m

ass

/ g

m-3

0

500

1000

1500

2000 [benzene], 40 x [NO

], 40 x [NO

2 ] / ppbv

Effect of NOx on p-Xylene SOA

0

5

10

15

20

25

30

35

40

9 10 11 12 13 14 15 16 17

hour

aero

sol m

ass

/ g

m-3

0

100

200

300

400

500

600

700[p-xylene], 3 x [N

O], 2 x [N

O2 ] / ppbv

Effect of NOx on Mesitylene SOA

0

5

10

15

20

25

30

35

40

9 10 11 12 13 14 15 16

hour

aero

sol m

ass

/ g

m-3

0

50

100

150

200

250

300[1,3,5-T

MB

], [NO

], 0.5 x [NO

2 ] / ppbv

Effect of NOx on Toluene SOA

0

2

4

6

8

10

0 20 40 60 80 100 120

aerosol concentration / g m-3

low-NOx

mid-NOx

high-NOx

Other toluene SOA mass concentration data and the role of NO

0

2

4

6

8

10

12

14

0 50 100 150 200 250

aerosol mass / g m-3

areo

sol y

ield

/ %

RO2. + NO RO. + NO2

HO2. + NO OH + NO2

RO2. + HO2. ROOHROOH adduct

Comparing datasets of toluene SOA yields

point of reference = SOA yield at 50 g m-3 aerosol loading

0

1

2

3

4

5

6

0 5 10 15 20

[toluene]0/[NO]0

aer

oso

l yie

ld /

%

NOx-free, limiting yield

SOA Forming Propensity of other Aromatics

0

1

2

3

4

5

6

7

0 20 40 60 80 100 120

aerosol concentration / g m-3

aero

sol y

ield

/ %

low-yield curve

high-yield curve

1,3,5-trimethylbenzene

toluene

1,2,4-trimethylbenzene

Can we relate variations in SOA yield to differences in gas-phase chemistry?

Unsaturated aldehydes are reactive in terms of indicated association chemistry

OH

OO

.O

O O

O

O

+ HO2

O O

OO

+ HO2

O O

O O

+ HO2

decomposition

O2

'Peroxide-bicyclic' route

[0.18]

[0.18]

[0.64]

Variations in SOA yield (Aromatics)

0

0.5

1

1.5

2

2.5

3

3.5

4

4.5

0 0.2 0.4 0.6 0.8

primary unsaturated aldehyde yield

aero

sol y

ield

/ %

Extension to the entire MCM

124 parent VOCs (MCM v3)

ca. 12600 chemical reactions

ca. 4500 chemical species

ca. 2000 closed-shell species with Tb(estimated) > 450 K

need to define 2000 new species,2000 phase-equilibria

Which are the most important components of simulated SOA?

Which are the most important SOA precursors?

Partitioning coefficients?

(pseudo-) Lagrangian, well-mixed boundary layer, chemical box model

Background anthropogenic and biogenic emissions throughout (NAEI)

Enhanced anthropogenic emissions for 3 hours

Idealised “trajectory”

Primary emitted OA

Background organic aerosol

Preliminary (Box) Modelling

A

B

Day 0

Day x

hour0 3 X

1

10

Ant

hrop

ogen

ic

Em

issi

on f

acto

r

Preliminary (Box) Model Simulations

Scaling factor = 50

0

0.2

0.4

0.6

0.8

1

1.2

1.4

1.6

0 1 2 3 4 5 6

Day (starting from 8 am)

g

m-3

Background organic aerosol

Secondary organic aerosol

Primary organic aerosol

Preliminary (Box) Model Simulations

Which are the most important SOA precursors?

O2N NO2

OH

O2N NO2

OH

Which are the most prevalent SOA components?

OH

HO

HOO

NO2

ONO2

OO

OO

NO2

OH

Conclusions and Further Work

Gas-aerosol partitioning (equilibrium) coefficients have been estimated for ca. 2000 species within the MCM v3.1.

Validation simulations have been performed using measured SOA data for the photooxidation of (-pinene) benzene, toluene, p-xylene and mesitylene.

These simulations strongly imply the key role of condensed organic-phase association chemistry.

Simulations further suggest the important role of ROOH. effect of NOx concentration.

To do:-

Model-measurement comparisons – scaling factors?; NOx?

Speciation of simulated SOA for low-NOx conditions

Simulated aerosol material dominated by five species:-

OH

O

O

O

OH

OH

O

O

O

O

O

HO

O

OHOH

O OH

O O O

O

O

OH

O

OH

O

In aerosol peroxyhemiacetal formation

ROOH + HC(=O)R’ ROOC(OH)R’H

H abstraction OH addition

.OO

O2

.O

O

+ HO2

O2

NONO

organic nitrate

OH

OO.OH

O2O2

'Phenolic' route

organic nitrate

NO

OH

O

O

OH

O

O

.OO

organic nitrate

NONO

OH

O

O

.O

OH

O.

O

isomerisation

isomerisation

O2

OH

O

O

O

O

O+ HO2

decomposition

O2

'Epoxy-oxy' route

O O

OO

O O

O

O

+ HO2

+ HO2

O O

OO + HO2

O O

O

O+ HO2

O O

OO

+ HO2

decomposition

O2

'Peroxide-bicyclic' route

(0.07)

(0.65)

(0.10)

(0.18)

Peroxyhemiacetal forming chemistry

OH

O

O

O

OH

O

O

OH

O

OH

O

O

O

HO

O

OHOH

Amended Catechol (1,2-dihydroxybenzene) Chemistry

HO

HO

O2N

HO

HO

O

O

OO

HO

O O

HO

HO

HO

HO

NO2

O O

OO

HO

HO OH

HO

0.06 0.800.14

0.20 0.80

Similar toMCM v3.1a