i EFFECT OF GREEN LEAF VOLATILES (GLVs) ON SECONDARY ORGANIC AEROSOL FORMATION Andebo Abesha Waza MSc thesis in Atmosphere-Biosphere studies Department of Applied Physics Faculty of Science and Forestry University of Eastern Finland November 2014 ii UNIVERSITY OF EASTERN FINLAND, Faculty of Science and Forestry Department of Applied Physics ANDEBO ABESHA WAZA: Effect of Green Leaf Volatiles (GLVs) on secondary organic aerosol formation. MSc thesis: 60 pages, 3 appendixes (18 pages) Supervisors: Jorma Joutsensaari, D.Sc. (Tech.), Docent and Pasi Yli-Pirila, MSc November 2014 _______________________________________________________________________________ Key words: Aerosol particles, secondary organic aerosol, ozonolysis, biogenic volatile organic compounds, green leaf volatiles, monoterpenes, formation rate, growth rate, yield, hygroscopicity ABSTRACT Climate change is one of the biggest challenges facing the world in the 21st century. Human activities, like combustion of fossil fuel result in emissions of different radiation-modifying substances like aerosol particles and greenhouse gases that have a profound influence on our climate system through either by warming or cooling earth's surface. Secondary organic aerosol (SOA) particles, which are formed by nucleation and condensation processes, accounts for a greater fraction of atmospheric aerosol particles and thus, it is important to have detailed understanding of SOA formation, properties and transformation processes and thereby to assess the impact on earth’s climate system and health effects. Green leaf volatiles (GLVs) are an important component of biogenic volatile organic compounds (BVOCs) released by vegetation during mechanical damage, herbivory attack, pathogen infection and abiotic stress. They play a major role in contributing to the formation of secondary organic aerosol particles in atmosphere. Reaction chamber experiments have been conducted to investigate SOA formation from ozonolysis of three major GLV compounds: trans-2-hexenal, cis3-hexen-1-ol and cis-3- hexenylacetate by using series of experiments performed in humid conditions (~50% RH). Similar experiments were also conducted with α-pinene and mixtures of terpenes (αpinene, sabinene, limonene, β-myrcene, ocimene, linalool and β-caryophyllene) as well as mixtures of GLVs and terpenes. We found that ozonolysis of VOCs emitted from green leaf plants play a very important role in new particle formation in chamber when they appear as a mixture with terpenes, whereas ozonolysis of GLVs alone is less effectively involved in particle formation. We also instigated that ozonolysis of monoterpenes (MTs) produced the highest SOA mass concentrations and GLVs produced the lowest while mixture of MTs and GLVs being intermediate indicating that monoterpenes plays a constitutive role during SOA formation process while GLVs have a suppressing effect on SOA formation. We have also studied the hygroscopic growth of SOA particles and found that SOA particles have low hygroscopicity showing very low water uptake with growth factor values in between 1.01-1.03. iii ACKNOWLEDGMENTS First and foremost, my utmost heartfelt gratitude goes to my main supervisor Jorma Joutsensaari (D.Sc. Tech., Docent) for his unquestionable and continual support, valuable comments and patience. Throughout this work, no matter how many times I came into his office without any appointment, I cannot remember a single day that he said, "Sorry, I am busy.” I am extremely lucky to have him as my thesis supervisor. I owe my special thanks to my second supervisor Pasi Yli-Pirila, MSc. His guidance in laboratory greatly helped me to complete my thesis successfully. I benefited a lot from his expertise in the laboratory work. I would like to extend my gratitude to Annele Virtanen (Associate Professor) for funding the experimental part of this research. I would like to extend my thanks to my examiner Prof. Jarmo Holopainen. I must also thank Kim Jaeseok (post doc) for all support and information he provided on topics related to H-TDMA measurements. I would like to express my appreciation to coordinator of Master's programme, Jussi Malila, MSc. His continues academic guidance and administrative interventions whenever I asked him helped me a lot to complete my study successfully. I'm so grateful for all his helps. I owe sincere and earnest thankfulness to my friend Mengistu Mengesha for his unwavering friendship over the years. His unparalleled support and unwavering encouragement over the past two years were sources of my strength. Without his helps, it couldn’t have been possible to complete my study. I am also very grateful to the department of applied physics for providing me all research facilities to carry out the work. Above all, my greatest thanks goes to the omnipresent God for giving me strength and determination to complete my study successfully. iv ABBREVIATIONS 1. BSOA: Biogenic Secondary Organic Aerosol 2. BVOC: Biogenic Volatile Organic Compounds 3. CCN: Cloud Condensation Nuclei 4. CPC: Condensation Particle Counter 5. DMA: Differential Mobility Analyzer 6. DMS: Dimethyl sulfide 7. GF: Growth Factor 8. GLVs: Green Leaf Volatiles 9. H-TDMA: Hygroscopic Tandem Differential Mobility Analyzer 10. IPCC: Intergovernmental Panel on Climate Change 11. MT: Monoterpene 12. NPF: new particle formation 13. OH: Hydroxide radical 14. PTR-MS: Proton-Transfer-Reaction Mass Spectrometer 15. RH: Relative Humidity 16. SMPS: Scanning Mobility Particle Sizer 17. SOA: Secondary Organic Aerosol 18. TME: tetramethylethylene 19. VOC: Volatile Organic Compounds v TABLE OF CONTENTS ABSTRACT ........................................................................................................................................ii ACKNOWLEDGMENTS ................................................................................................................iii ABBREVIATIONS ........................................................................................................................... iv LIST OF FIGURES .........................................................................................................................vii LIST OF TABLES ..........................................................................................................................viii Chapter 1: BACKGROUND ............................................................................................................. 1 1.1 Introduction ........................................................................................................................... 1 1.2 Aim of study .......................................................................................................................... 2 1.3 Research questions ................................................................................................................ 2 1.4 Thesis outline ........................................................................................................................ 2 Chapter 2: LITERATURE REVIEW .............................................................................................. 3 2.1 Secondary organic aerosol (SOA) formation and its general properties .................................... 4 2.2 Biogenic volatile organic compounds ........................................................................................ 6 2.3 Green leaf volatiles as a global source of biogenic secondary organic aerosol ......................... 6 2.4 Instruments for aerosol size distribution measurement .............................................................. 8 2.5 Hygroscopicity of SOA particles ............................................................................................... 8 Chapter 3: MATERIALS AND METHODS ................................................................................. 10 3.1 Reaction chamber ..................................................................................................................... 10 3.2 Reagents and Chemicals ........................................................................................................... 12 3.3 Aerosol size distribution measurement .................................................................................... 12 3.4 Monitoring VOC change .......................................................................................................... 13 3.5 Tandem Differential Mobility Analyzer (H-TDMA) measurements ....................................... 15 3.6 Calculation of SOA mass yield ................................................................................................ 15 3.7 Overview of the experiments ................................................................................................... 16 vi Chapter 4: RESULTS AND DISCUSSION ................................................................................... 17 4.1 Analysis of aerosol characterization......................................................................................... 18 4.1.1 Blank chamber tests ........................................................................................................... 18 4.1.2 Particle formation and growth measurements ................................................................... 18 4.2 SOA mass concentration and yield analysis............................................................................. 28 4.3 Growth Factor (GF) values....................................................................................................... 31 Chapter 5: CONCLUSIONS AND RECOMMENDATIONS ..................................................... 36 5.1 Conclusions .............................................................................................................................. 36 5.2 Recommendation for further research ...................................................................................... 37 REFERENCES ................................................................................................................................. 38 APPENDIXES .................................................................................................................................. 42 vii LIST OF FIGURES Figure 1: Schematic picture of SOA formation ................................................................................... 5 Figure 2: Picture indicating causes of GLV emission.......................................................................... 7 Figure 3: Reaction chamber ............................................................................................................... 11 Figure 4: SMPS experimental setup during ozonolysis experiment .................................................. 13 Figure 5: PTR-MS machine used in our experiment ......................................................................... 14 Figure 6: Schematic representation of H-TDMA experimental setup .............................................. 15 Figure 7: SOA formation from ozonolysis of cic-3-hexenol experiment .......................................... 20 Figure 8: SOA formation from ozonolysis of 3-hexenyl acetate experiment .................................... 21 Figure 9: SOA formation from ozonolysis of α-pinene experiment .................................................. 24 Figure 10: SOA formation from ozonolysis of α-pinene and GLV-mix experiment ........................ 25 Figure 11: Plot of growth factor as function of time for ozonolysis of trans-2-hexenol ................... 33 Figure 12: Plot of growth factor as function of time for ozonolysis of α-pinene .............................. 34 Figure 13: Plot of growth factor as function of time for ozonolysis of MT-mix and GLV-mix ....... 35 viii LIST OF TABLES Table 1: Overview of the experiments ............................................................................................... 16 Table 2: Analysis of particle total concentration (Ntot), formation rate and growth rate ................... 23 Table 3: Summary of literature values showing particle number concentration and growth rate observed at different locations across the globe ................................................................................ 27 Table 4: Analysis of VOC consumption, ozone conc. change over time, ΔM tot max and SOA yields ............................................................................................................................................................ 29 Table 5: Summary of the mean values of growth factor (GF) values for some selected dry particle sizes .................................................................................................................................................... 32 ix x 1 Chapter 1: BACKGROUND 1.1 Introduction Atmospheric aerosols, which are liquid or solid particles suspended by carrier gas (air), play an important role in environmental and atmospheric processes. For instance, they take part in heterogeneous chemical reactions in the atmosphere which affects the distribution and the abundance of trace gases in atmosphere (Andreae and Crutzen, 1997; Haywood and Boucher, 2000). Aerosol particles can also influence the climate system by changing the earth’s energy budget in several ways. For example, they can scatter and absorb the radiation directly (the direct effect) (Haywood and Boucher, 2000). Aerosol particles can also act as cloud condensation nuclei (CCN), around which clouds can form (which is known as the indirect effect) which modifies the radiative properties, the amount and the lifetime of clouds (Haywood and Boucher, 2000). In light of these, it has been said that aerosol particles evidently affect the radiative balance in earth’s atmosphere and hence they play a major role in Earth’s climate system (IPCC, 2007). Secondary organic aerosol particles (SOA) are formed from condensation of low volatility compounds by chemical oxidation from both biogenic and anthropogenic volatile organic compounds (Robinson et al., 2007). Plants are the largest contributor to the organic fraction of atmospheric fine particulate matter, which can be through direct emissions or through SOA formation (Seinfeld and Pandis, 1998). Despite improvements in study of SOA formation, many of the basic processes governing formation, growth, chemical and physical properties of SOA particles are still poorly understood. Recent studies on estimate of global secondary organic aerosol production based on VOC flux expected that there could be significant missing SOA precursors that are currently unknown (Goldstein and Galbally, 2007). Thus, it is suspected that the Green leaf volatiles (GLVs) could be important parts of the missing global source of SOA. Moreover, in most chamber studies, only single organic precursors (typically α-pinene or toluene) are used as exemplary compounds to study the SOA formation (Hao et al., 2009). However, since the mechanism of SOA formation involves complex steps, it is very much unclear as to what degree the results obtained from single monoterpene chamber studies could be generalized to the actual atmospheric conditions (Van Reken et al., 2006). Therefore, we believe that more realistic and important information can be obtained if we extend our studies to green leaf volatiles. 2 1.2 Aim of study The main objective of this chamber study was to examine the SOA formation from ozonolysis of various GLVs (trans-2-hexenal, cis-3-hexenol and 3-hexynyl acetate) by using series of chamber experiments performed in humid conditions (~50% RH). Similar experiments were also conducted with α-pinene and mixtures of monoterpenes (MT, α-pinene, sabinene, limonene, β-myrcene, ocimene, linalool and β-caryophyllene) and then the results were used as a reference. Furthermore, experiments with mixtures of GLV and MT were conducted. The SOA formation yields obtained from ozonolysis of GLVs were then compared to those obtained from α-pinene and MT-mixture. In order to examine the water absorbing capacity, the study also examined the hygroscopicity of SOA particle produced and the results were compared with the literature values. 1.3 Research questions 1. How does the VOC emission profile affect the secondary organic aerosol formation? 2. Can GLVs suppress the secondary organic aerosol formation in chamber study? 3. How hygroscopic are SOA particles those which generated from ozonolysis of GLVs and how would hygroscopicity of SOA particles whose precursors are GLVs be compared to SOA particles whose precursors are monoterpenes and other inorganic species? 1.4 Thesis outline The overall structure of the thesis is organized in five chapters. The first chapter introduces the general background of study, research frame, objective and significance of the study as well as research questions. Chapter two deals with literature review. In this section more detailed description of the research topics is covered. In chapter three, materials and methods are briefly discussed. In chapter four, results and discussion are clearly presented. In this session, results of size distribution measurement, yield calculation and growth factor values are discussed in detail. Finally, chapter five presents conclusions and recommendation remarks based on the main findings of the study. 3 Chapter 2: LITERATURE REVIEW There seems to be strong evidence that the Earth's climate is now changing. Human activities take greater share of climate change problem by causing changes in the amounts of the greenhouse gases, aerosols, and cloudiness on atmosphere which can significantly modify the earth’s energy balance either warming or cooling the climate system. This could lead to several severe and irreversible problems if no proper action (such as adaptation and mitigation strategies) is to be taken. According to the IPCC (2007) report, the largest range of uncertainty in the radiative forcing is coming mainly from the direct and indirect aerosol effect on climate change. The net effect of aerosols on earth’s climate is to cooling the climate system directly by reflecting the incoming sunlight back to space, and also indirectly by increasing the brightness and cover of clouds that in turn also reflect more sunlight to space again (Kaufman, 2006). In addition to affecting the climate, atmospheric aerosols can also cause adversarial health effects such as premature death, increases in respiratory illness, and cardiopulmonary mortality (Laden et al., 2000). Therefore to decrease the negative impacts for the present and future generations it is inevitable to study aerosols, to know their formation and growth mechanism in atmosphere, sources, and chemical composition as well as their physical and chemical properties. Aerosol particles can be either emitted as primary aerosols (such as dust or soot particles) or they can also be formed by chemical reactions from the condensation and gas-particle partitioning in atmosphere. Sources of aerosols could be either natural (e.g. mineral and volcanic dust, sea salt, dimethyl sulfide (DMS), volcanic sulfur dioxide (SO2), biogenic volatile organic compounds) or manmade (such as soot, SO2 from fuel combustion, nitrogen oxides (NOx), anthropogenic volatile organic compounds) (Seinfeld and Pandis, 2006). Aerosol particles can also vary in size ranging from nanometers up to few micrometers in diameter (Raes et al., 2000). Similarly, the concentration could also differ interim of spatial and temporal distribution. For example, the number concentration of aerosol particles can range from 10-100000 particles per cm-3 and similarly its mass concentration can vary from 0.1μgm-3 (in rural or unpolluted regions) to100μgm-3 in urban (polluted regions) (Seinfeld and Pandis, 2006). 4 2.1 Secondary organic aerosol (SOA) formation and its general properties Organic aerosol is the most important part of submicron particles (Zhang et al., 2007). It can exist in particle phase as primary organic aerosol or secondary organic aerosol (Robinson et al., 2007). Organic aerosol particles significantly contribute to the total fine aerosol mass at both continental midlatitudes and tropical forested areas (Seinfeld and Pankow, 2008). SOA particles are formed in atmosphere by chemical reaction from condensation and gas-particle partitioning of semivolatile products of hydrocarbon oxidation species (i.e. OH, O3 and NO3) (Kanakidou et al., 2005). Kanakidou et al. (2005) also reported that 60% of organic aerosol mass on the global scale is secondary organic aerosol while at regional level; they even estimated it to be higher than the reported global amount. This indicates aerosol concentration is largely due to secondary particle production in atmosphere. And therefore, detailed understanding of SOA formation process is important to assess its impact on earth’s climate system. Several studies have been conducted in the last few years to better understand the formation and evolution of organic aerosols in atmosphere (Kroll and Seinfeld, 2008). However, there are still uncertainties regarding the formation of SOA via the oxidation products (Hallquist et al., 2009). For example, one of the problems associated with SOA formation from VOC oxidation in the gas phase is that each VOC can undergo a number oxidation processes to produce different oxidized products, which may or may not necessarily contribute to formation and growth secondary organic aerosol (Hallquist et al., 2009). Moreover, once they are formed, SOA particles can undergo coagulation, structural rearrangement and also phase transition which makes SOA formation process more complex (Fuzzi et al., 2006). Relative humidity, concentration of organics and oxidants, rate constants for oxidation, absorption ability, properties of the species and the ability to form solutions with compounds already present in the aerosol phase are among the factors known to affect the SOA formation (Ervens and Kreidenweis, 2007). About 85-90% of secondary organic aerosol particles are produced mainly from oxidation of biogenic precursors (Stavrakou et al., 2009). Figure (1) shows the schematic of SOA formation paths and its growth mechanism from semivolatile oxidation products. 5 Figure 1: Schematic picture of SOA formation (Source: Griffin et al. 2005) Chung and Seinfeld (2002) indicated that 91% of SOA formation is caused by O3 and OH oxidation while Kanakidou et al. (2005) suggested that ozonolysis dominates SOA production when compared to OH and NOx oxidation. Similarly, Bonn et al. (2002) also reported that ozone has the highest potential to form new particles by nucleation through reaction with α-pinene. 6 2.2 Biogenic volatile organic compounds Volatile organic compounds (VOCs) are generally compounds that are capable of vaporizing into the atmosphere under normal temperature and pressure. They have sufficiently high saturation vapor pressure that enables them to evaporate (either partly or completely) to the atmosphere. The sources can be either biogenic or anthropogenic; however, the biogenic VOCs represent greater part of the total VOC emissions (Guenther et al., 1995). Terrestrial biosphere is the main source of the biological volatile organic compounds (BVOCs) and it provides a link between the earth’s surface and atmosphere (Dudareva et al., 2006). BVOCs can cause a significant effect on the chemical composition and physical characteristics of the earth’s atmosphere (Laothawornkitkul et al., 2009). For example, they can affect atmospheric oxidation cycles such as ozone formation and formation of secondary organic aerosol particles (Riipinen et al., 2011). Plants release different kinds of biogenic volatile organic compounds (BVOCs) into the atmosphere. Some of these chemical species can be classified as terpenoids (e.g., isoprene, monoterpenes, and sesquiterpenes) while others can be classified as non-terpenoids (such as methanol, acetaldehyde, and acetone) (Kesselmeier and Staudt, 1999). Among oxygenated organic compounds categorized as plant emissions: 1,8-cineole is known to be emitted from eucalyptus, linalool is identified to be emitted from orange blossoms while cis-3-hexen-1-o1 (leaf alcohol), cis-3-hexenenylacetate (leaf acetate), and trans-2-hexenal (leaf aldehyde) are emitted from grasses and other agricultural crops and are called green leaf volatiles (Arey et al., 1991). In the atmosphere, these oxygenated organic compounds react with OH radicals, NO3 radicals, and O3 (Atkison, 1988) and form secondary organic aerosols (Guenther et al., 1995). 2.3 Green leaf volatiles as a global source of biogenic secondary organic aerosol The green leaf volatiles (GLVs) are one of the most significant groups of these BVOCs and are a group of unsaturated oxygenated hydrocarbons which are produced from the biochemical conversion of linoleic and linolenic acid within plant cells (Hamilton et al., 2009). They are ‘wound-induced’ VOCs emitted to atmosphere by several plant species when plants undergo stress or mechanical damage (e.g. during grass cutting or grazing of animals and other stress factors such as herbivory 7 attack, pathogen infection (Hamilton et al., 2009). Local weather conditions (temperature change) can also cause the release of GLVs. For example, high concentrations of GLVs were emitted in the Alps after a freezing spell, and were then attributed to emission from damaged cells upon thawing (Karl et al., 2001). Variation in emission amount has also been reported among different ecosystems. For example, grasslands are estimated to emit up to 130 mg C m–2 GLVs annually, while the reactive lawn-GLV emissions are found to be 3.9 to 6.3 Gg C annually (Brilli et al., 2012). These emissions are said to be a significant source of VOCs in the atmosphere. Isoprene, monoterpenes, sesquiterpenes and methanol are the dominant compounds emitted under unperturbed conditions. Although the emission rates of GLVs are lower when compared to the emission rates of the more commonly studied isoprenoids, they are still considered to be an important group of chemicals (Arey et al., 1991; Konig et al., 1995). GLVs play a significant role in atmospheric chemistry and physics (Atkinson, 1997). For example, they can increase the levels of SOA in atmosphere over healthy plants (Joutsensaari et al., 2005) and thus are important aerosol precursors. Figure (2) indicates the causes of GLV emission from plants. Figure 2: Picture indicating causes of GLV emission (Source: Holopainen., 2014). 8 2.4 Instruments for aerosol size distribution measurement Nowadays, atmospheric particle formation and growth have received considerable attention. And as result, many advanced instrumental techniques for measuring concentrations of freshly formed particle have been developed (Raes et al., 1997). Particle formation and growth are the most important parameter to characterize the intensity of new particle formation (NPF) events. The scanning mobility particle sizer (SMPS) technique is one of the most commonly employed method for measuring particle size distribution (Sandip and David, 2005) and thus determination of particle formation rate and particle growth rate. Particle formation rate defines the number of particles formed in unit volume and time. On other side, since major aerosol effects depend on the diameter of aerosol particles, GR is one most important parameter to look into (Yli-Juuti et al., 2011). It measures an increases particle diameter unit time. In atmosphere, aerosol particles growth takes place mainly through selfcoagulation, coagulation scavenging and condensation (Leppä et al., 2011). Condensational growth is the condensation of vapors onto the pre-existing particles (Sarangi et al., 2013). Aerosol growth by coagulation is a kinetic process in which particles in in relative motion undergo collision with each other and fuse (Yu and Turco, 1998). 2.5 Hygroscopicity of SOA particles The capability of atmospheric aerosol to absorb water is one of important properties of aerosol particles. Water uptake affects the particle size as well as phase and therefore it influences the physicochemical characteristics of the aerosol particles, including optical properties of aerosols, atmospheric lifetime, and chemical reactivity (Heintzenberg et al., 2001). Moreover, water uptake property of aerosol particles can also define the capacity of aerosol particles to serve as a cloud condensation nucleus (CCN). And this leads to modification in both direct and indirect radiative forcing of the climate (IPCC, 2001). Hygroscopicity is the change in submicron particle size change due to water uptake by particles (Peter and Mark, 1989). It defines how aerosol particles interact with water vapor at different saturation conditions (McFiggans et al., 2006). In addition to their climatic relevance, the hygroscopicity of aerosols can bring an adverse impact on the human health associated with health effect of particulate matter (Stapleton et al., 1994; Davidson et al., 2005). As atmosphere contains both inorganic and organic species, thus we need to understand the hygroscopicity of both inorganic and organic species in atmosphere. However, there are still large uncertainties in our 9 understanding of the hygroscopicity of the organic species and these understanding gaps present further challenge in simulating aerosol indirect radiative forcing (Petters et al., 2009). Hygroscopicity of aerosol particles is commonly described in terms of particle size or mass changes as a function of relative humidity (RH) under some saturation conditions. There has been variety of experimental techniques that have been used to measure the hygroscopic growth of aerosol particles with its specific advantages and limitations. After introduced by Liu et al. (1978) for the first time, the TDMA technique has been used to study the change in particle size due to imposed aerosol processing (Swietlicki et al., 2008). And the technique have been commonly used to study the size change of particles associated with humidification (H-TDMA), evaporation (V-TDMA), chemical reactions (R-TDMA) and uptake of organic vapor (O-TDMA) (Swietlicki et al., 2008). H-TDMA has been mostly used over the last two decades to characterize the hygroscopic properties (i.e. size changes of submicron particles after a treatment such as exposure to high relative humidity) of atmospheric aerosol particles across the globe (Duplissy et al., 2008). The main aim of H-TDMA measurements is to obtain the distribution of growth factors (GF) exhibited by the particles of some selected dry particle size upon exposure to high RH (Swietlicki et al., 2008). The GF is defined as the ratio of the diameter of humidified particle (D(RH)) to that of the initial dry classified particle diameter (D0) at some well-defined relative humidity RH. GF =D(RH)/D0 (Swietlicki et al., 2008). Hygroscopicity of atmospheric aerosol particles can range from non-hygroscopic (i.e. such as primary organic aerosol which are directly emitted from fossil fuel combustion) to highly hygroscopic biomass burning organic aerosol particles (Petters et al., 2009). Hygroscopicity of secondary organic aerosols particles was reported in previous studies. For example, Varutbangkul et al. (2006) measured the GF values for SOA particles at 85% RH and found the values in between 1.09–1.16 from ozonolysis of cycloalkenes, 1.01–1.04 for photooxidation of sesquiterpene and 1.06–1.10 for the monoterpene and oxygenated terpene. Similarly, Virkkula et al. (1999) also measured the growth factor (GF) values for SOA particles at 85%RH using (NH4)2SO4 as seed particles and found GF value to be 1.1 from ozonolysis of α-pinene, β-pinene and limonene. Similarly, Saathoff et al. (2003) also measured GF values for SOA particle produced from ozonolysis of α-pinene (at 200 nm) and the reported value were: 1.106 at 85% RH for nucleated SOA, 1.55 for SOA with (NH4)2SO4 seed, 1.08 for SOA with diesel soot seed. 10 Chapter 3: MATERIALS AND METHODS 3.1 Reaction chamber The experiments were performed in 9.8m3 rectangular Teflon TM FEP film chamber (see figure 3) at Physics research laboratory (in Department of Applied Physics) at University of Eastern Finland during 06–23 May 2014. After cleaning, the chamber humidification was made by using the Perma Pure humidifier (Model FC-125-240-SMP, Perma Pure, and New Jersey) and heated water bath. The relative humidity (RH) was adjusted to be around 50 ± 5 %. Approximately 30-45 min was allowed for the RH value inside the chamber to reach 50% RH value. After attaining the 50% RH value, the ozone enriched air at a flow rate of 15 liter per minute was introduced into the chamber through a fitting that is connected the chamber horizontally. The ozone was produced by a UV light ozone generator (i.e. with wave length of 185nm). Ozone concentration in the chamber was controlled by a UV Photometric ozone analyzer (49i, Thermo Fisher Scientific Inc., MA) that samples air at a rate of 1.5 liter per minute. It took approximately 10-15 min for ozone generator to produce the ozone concentration level of our interest (200 ppb ±10%). Finally VOCs were injected by syringe into the reaction chamber. Carrier gas was used to introduce VOCs into the chamber. Ozonolysis reactions were performed when ozone concentration in chamber reaches about 200ppb ±10%. Clean air was supplied to the chamber by passing a compressed air through an air cleaning system that includes a homemade compressed air dryer to remove moisture and particles and other contaminates. All experiments were carried out under darkness to remove the possible photochemical effects. Before performing each experiment, the chamber was constantly flushed with laboratory compressed clean air until the chamber is clean of any particle. Similarly, after each of the experiments, cleaning of the chamber was performed. No radical scavenger or seed aerosol was used. 11 Figure 3: Reaction chamber 12 3.2 Reagents and Chemicals For our work, GLV solutions were prepared using commercially-available liquid green leaf volatiles which were bought from Sigma-Aldrich (Milwaukee, WI, USA) and received without any further purification. The GLVs used in this study were: trans-2-hexenal (98%), cis-3-hexanol (98%) and 3hexynyl acetate (98%). Furthermore, α-pinenene (99%) and mixtures of terpenes (α-pinene, sabinene, limonene, β-myrcene, ocimene, linalool and β-caryophyllene) were used in these experiments. Tetramethylethylene (TME; 99+%, Aldrich) was also added to the reaction chamber to initiate the production of the OH radicals inside the chamber after two GLV/MT addition. The main purpose of adding TME was to see the role of OH in the new particle production. TME was injected to the chamber by syringe containing some fixed volume of TME (about 10µl, 200ppb). As suggested by Lambe et al. (2007), OH radicals are produced when tetramethylethylene (TME) reacts with O3. 3.3 Aerosol size distribution measurement The formation and evolution of SOA during ozone exposure in the chamber was determined by the aerosol particle number size distribution measurement with a scanning mobility particle sizer, SMPS system (TSI long-DMA 3081). The SMPS consists of a TSI long-DMA 3081 Differential Mobility Analyzer (DMA) which is used to classify the aerosol particles based on their electrical mobility and a TSI Model 3775 Condensation Particle Counter (CPC) which is then used to measure the concentration of those size-classified particles (see figure 5). The DMA was operated with aerosol and sheath flows of 0.3 and 3.0 liter per minute, respectively to measure the size distribution of the particles in the 15–700 nm range. The size distributions were measured for every 3 min. Figure (4) shows our SMPS experimental setup. 13 Figure 4: SMPS experimental setup during ozonolysis experiment 3.4 Monitoring VOC change Besides the particle formation measurement, the VOC measurements were also conducted simultaneously with a Proton-Transfer-Reaction Mass Spectrometer (PTR-TOFMS, Ionicon Analytik GmbH, see Fig. 5) to determine the concentration change over time. PTR-MS has been widely used to study the link between new particle formation and VOC concentration change (Jordan et al 1995). It is a very sensitive technique for online monitoring of VOCs in ambient air and is developed by scientists at the Institut für Ionenphysik at the Leopold-Franzens University in Innsbruck, Austria (Jordan et al 1995). A typical PTR-MS instrument consists of four components (1) an ion source that 14 is directly connected to a drift tube, (2) a drift tube (3) an ion transfer chamber (4) an ion an analyzing system (time-of-flight mass spectrometer). For off-line analysis, the VOCs were sampled onto about 150mg Tenax TA adsorbent (Supelco, mesh 60/80) for 15-20 min and analyzed with thermo desorption gas-chromatograph mass spectrometer. Figure 5: PTR-MS machine used in our experiment 15 3.5 Tandem Differential Mobility Analyzer (H-TDMA) measurements H-TDMA measurements have also been conducted in chamber to investigate the water uptake properties of secondary organic aerosol particles generated by ozonolysis of GLVs and monoterpenes. H-TDMA consists of Vienna type, short DMA and a TSI 3025 CPC. The flow rates of aerosol and sheath air were 1 and 6 liter per min respectively and was operated at constant high RH value of approximately 90%. The measured particle size was 30, 50, 100, 150 nm depending on particle concentration. DMAs had a closed-loop sheath air circulation system. Relative humidity of sample aerosol and excess air in DMA 2 were measured with a capacitive sensor (VaisalaHMP110) and a dew point meter (Dewmaster), receptively. Finally the GF values obtained in this work were compared with existing values in the literatures. And in doing this, the agreement of our work to the previous works was evaluated. Figure (6) shows the schematic representation of H-TDMA experimental setup. Figure 6: Schematic representation of H-TDMA experimental setup 3.6 Calculation of SOA mass yield 16 SOA mass yield (Y) is commonly obtained by calculating the ratio of the total aerosol mass concentration Mo (in μgm−3) to the amount of total precursor VOCs reacted (in μgm−3) at the end of every experiment. That is: Y=Mo∕ΔVOCs (Jay et al., 1996). The type of organic precursor molecules and the mass of organic aerosol are among other factors known to affect the yield of SOA particles. To our knowledge, there was very limited study conducted on SOA yield obtained from ozonolysis of green leaf volatiles. In this work, we calculated the mass yield of the secondary organic aerosol particles produced from ozonolysis of the GLVs and then obtained result was again compared to those obtained from α-pinene as reference. Furthermore, experiments with a mixture of GLV and MT were also carried out. The aerosol yield is calculated from size distribution measurement made with SMPS and gases concentrations measured with PTR-MS. 3.7 Overview of the experiments We performed 13 experiments – three with only GLVs and two were only for MTs while the rest are the mixture of GLVs and MT. Table (1) summarizes all the experiments that we conducted in the laboratory. During these ozonolysis experiments, we were also interested to know whether the concentration VOCs affects the aerosol formation and growth and thus we injected more GLVs in the second injection round. The concentration of MT was held constant (40ppb) during the time when more GLVs were injected to the reaction for second time. The concentration of GLVs was between 2µl-2.6µl (40ppb-41ppb). For all of experiments, injection of VOCs for second time performed around in between 10:20-11:00. Table 1: Overview of the experiments 17 Exp. Exp. days numbers Terpenes GLV(ppb) (ppb) O3 (ppb) O3 (ppb) during during the first the second inj. RH (%) inj. 1 7.5.2014 - trans-2- 44 42 50 219 195 50 204 182 50 hexenal_40+40 2 8.5.2014 - cis-3-hexenol _40+40 3 9.5.2014 - 3-hexynyl acetate_40 +40 4 12.5.2014 a-pin_40 - 212 185 50 5 13.5.2014 a-pin_40 trans-2-hexenal 201 177 50 201 155 50 210 167 50 223 190 50 - 210 127 50 MT-mix trans-2-hexenal 209 199 50 _40 _40+40 MT-mix cis-3-hexenol 210 178 50 _40 _40+40 MT-mix 3-hexynyl acetate 225 185 50 _40 _40 +40 MT-mix GLV-mix 40+40 215 189 50 _40+40 6 14.5.2014 a-pin_40 cis-3-hexenol _40+40 7 15.5.2014 a-pin_40 3-hexynylacetate _40 +40 8 16.5.2014 a-pin_40 GLV-mix_40+40 9 19.5.2014 MT-mix _40 10 11 12 13 20.5.2014 21.5.2014 22.5.2014 23.5.2014 _40 Chapter 4: RESULTS AND DISCUSSION 18 4.1 Analysis of aerosol characterization In this section, we present results from chamber studies of new particle formation from ozonolysis of green leaf volatiles and monoterpenes. As already mentioned in the introduction part, monoterpenes were used for comparison purpose. Figures in appendix (A1.1-A1.8) characterize a contour plot of aerosol particle number size distributions, total aerosol particle number and mass concentration, ozone concentrations and VOC concentration during ozonolysis of GLVs and MTs. 4.1.1 Blank chamber tests Blank chamber tests were performed before each ozonolysis experiment. During this blank chamber tests, we measured particle and VOC concentration before adding any ozone or VOC to make sure that chamber was clean at the beginning of the each experiment. The main importance of this blank chamber test was because we believe that the volatile organics that were injected into the reaction chamber could be adsorbed on chamber walls and thus it would react with ozone during ozonolysis experiment forming new particles. We recorded the background particle concentration and mass concentrations. We disregarded the effects of NOX and SO2 in our works as their concentration was negligible (i.e. each with concentrations lower than 0. 1 ppb). The test was performed prior to beginning of ozonolysis experiment. The average particle concentration counted during this blank chamber test was very small (approximately 50 #/cm3) which is arguably insignificant. Thus we concluded that there was no significant particle formation detected during this chamber ozonolysis. The absence of new particle formation during this blank chamber test indicates that SOA formation observed during ozonolysis experiments were due to ozonolysis of GLVs and MTs compounds injected into the reaction chamber but not because of impurities adsorbed on the chamber walls. 4.1.2 Particle formation and growth measurements In this section, we describe the variability in new particle formation over ozonolysis of different green leaf volatiles and monoterpenes. Both growth rate and particle formation rates are calculated from 19 SMPS data. Several methods have been used for calculating aerosols growth rates from atmospheric observation, however, in this work; we used the geometric mean diameter to characterize the growth rate. On the first day experiment (i.e. ozonolysis of trans-2-hexenal), particle formation was not detected. However, clear new particle formation was detected during ozonolysis of cis-3-hexenol and 3hexenyl acetate. For instance, particle formation rate detected when cis-3-hexenol reacted with ozone was about 1.98 cm−3 s−1 while it was about 0.22 cm−3 s−1 in the case of ozonolysis of 3-hexenyl acetate. The particle growth rates, on the other hand, were also found to be 27nmh−1 and 18nmh−1 respectively. The lowest growth was observed for ozonolysis of 3-hexenyl acetate (about 17.8 nmh−1). But generally when compared to MTs, weak SOA particle formation event was observed during ozonolysis of GLVs. Figures (7 and 8) show the plot SOA formation from ozonolysis cis-3-hexenol and 3-hexenyl acetate respectively. We believe that during ozonolysis, the fragmentation of the precursors to more volatile products which cannot produce SOA could be the main reason for why there is weak SOA formation from ozonolysis of pure GLVs when compared to MTs. For example, Harvey et al. (2014) suggested that ozonolysis of linear alkenes produce less SOA because their fragmentation products are too volatile to enter the particle phase. Moreover, it is observed that ozonolysis of cis-3-hexanol produced more SOA particles than ozonolysis of 3-hexenyl acetate. The main explanation for why ozonolysis of cis3-hexanol produced more SOA particles than ozonolysis of 3-hexenyl acetate is because of in the case of ozonolysis of cis-3-hexanol, there may be more SOA particles as reaction product than in the case of ozonolysis of 3-hexenyl acetate. Moreover, we would suspect that the difference in the reaction rate with ozone could also resulted in difference in SOA formation between cis-3-hexanol and 3-hexenyl acetate. For example, Atkinson et al (1995) investigated that reaction constant for cis3-hexen-1-ol when it reacts with ozone was about (6.4 ± 1.7) × 10−17 cm3 molecule−1 s−1 while the reaction constant of cis-3-hexenylacetate for reaction with O3 about (5.4 ± 1.4) × 10−17 cm3 molecule−1 s−1. 20 Figure 7: SOA formation from ozonolysis of cic-3-hexenol experiment (From top to down-a contour plot of aerosol particle number size distributions (measured with the SMPS), aerosol particle number (from SMPS results), total organic mass (Mtot), ozone (O3) and VOC concentrations) 21 Figure 8: SOA formation from ozonolysis of 3-hexenyl acetate experiment (From top to down-a contour plot of aerosol particle number size distributions (measured with the SMPS), aerosol particle number concentrations (from SMPS results), total organic mass concentration (Mtot), ozone (O3) concentration and VOC concentration). During ozonolysis of MTs, more intensive SOA particle formation was observed at beginning stages of reaction and then growth continued as far as VOCs are there to react with ozone (see figure 9 and 10). For example, in ozonolysis of pure α-pinene, we found that the particle formation rate as high as 224 cm−3 s−1. However, it has been also seen that SOA formation decreases when α-pinene mixed 22 with pure GLVs or mixture of GLVs. The particle formation for α-pinene reduced from 224 cm−3 s−1 to about 33 cm−3 s−1 when α-pinene is mixed with GLVs. It was also observed that the particle formation rate in ozonolysis of MT-mix was higher when compared to the ozonolysis of GLVs alone. Moreover, because of the involvement of α-pinene, which is more responsible for nucleation, the particle formation rate observed during ozonolysis of the mixture of α-pinene and cis-3-hexenol was approximately 40 times higher than that in ozonolysis of pure cis-3-hexenol and also this trend was consistent with ozonolysis of and cis-3-hexenol. But the particle formation rate when α-pinene mixed with cis-3-hexenol was higher than pure ozonolysis of cis-3-hexenol. Similarly, on average more growth rate was observed in the case of ozonolysis of GLVs when they were mixed with MTs than when they react with ozone alone. The particle growth rates observed in these experiments was in the range of 21 nmh−1-42 nmh−1. A similar growth rate was obtained for ozonolysis of MTs (α-pinene and MT-mix). The maximum growth (42 nmh−1) was found when α-pinene was mixed with 3-hexynyl acetate while the minimum growth rate was detected during ozonolysis of 3-hexynyl acetate. Ozonolysis of pure α-pinene has more particle formation rate (224 cm−3 s−1) when compared to particle formation rate of pure MTs (129cm−3 s−1). The main explanation for difference in particle formation rate between α-pinene and MTs is that some of the compounds in the mixture of MT could not be easily reacting with O3 and as the result, the particle formation in the mixture of MTs could be lower than the pure α-pinene. Generally, the implication of these results is that ozonolysis of VOCs emitted from green leaf plants play a very important role in nucleation process through suppressing the SOA formation. See the summary of particle formation rate, growth rate and total particle concentration (Ntot max) in table (2). 23 Table 2: Analysis of particle total concentration (Ntot), formation rate and growth rate N tot max Formation rate Growth rate (cm -3s-1) (nmh-1) Exp.date MT GLVs 07-05-2014 -------------- trans-2-hexenal N/A N/A N/A 08-05-2014 --------------- cis-3-hexenol 4350 2 27 09-05-2014 -------------- 1370 0.2 18 12-05-2014 α-pinene ----------------- 89600 224 35 13-05-2014 α-pinene trans-2-hexenal 49900 198 36 14-05-2014 α-pinene cis-3-hexenol 35500 76 33 15-05-2014 α-pinene 32100 33 42 16-05-2014 α-pinene GLV-mix 43800 54 39 19-05-2014 MT-mix ---------------- 26700 129 33 20-05-2014 MT-mix trans-2-hexenal 99600 184 28 21-05-2014 MT-mix cis-3-hexenol 76300 104 27 22-05-2014 MT-mix 150000 471 22 23-05-2014 MT-mix 127000 295 23 3-hexynyl acetate 3-hexynyl acetate 3-hexynyl acetate GLV-mix (#/ cm3) 24 Figure 9: SOA formation from ozonolysis of α-pinene experiment (From top to down-a contour plot of aerosol particle number size distributions (measured with the SMPS), aerosol particle number concentrations (from SMPS results), total organic mass concentration (Mtot), ozone (O3) concentration and VOC concentration) 25 Figure 10: SOA formation from ozonolysis of α-pinene and GLV-mix experiment (From top to down-a contour plot of aerosol particle number size distributions (measured with the SMPS), aerosol particle number concentrations (from SMPS results), total organic mass concentration (Mtot), Ozone (O3) concentration and VOC concentration) The maximum particle concentration found in these days was about 150000 particle cm−3 (during ozonolysis of MT-mix and 3-hexynyl acetate) while the minimum particle concentration was about 26 1370 particle cm−3 (ozonolysis of 3-hexynyl acetate). Generally, lower particle number concentration was obtained from ozonolysis of GLVs when compared to MTs. But mixing MTs with GLVs during ozonolysis decreased total number concentration when compared to ozonolysis of ozonolysis of pure MTs. For example, the maximum total number concentration obtained during ozonolysis of pure αpinene was about 89600 particle cm−3 but when α-pinene was mixed with GLV-mix, the particle number concentration decreased to 43800 from 89600 particle cm−3. Since fragmentation products of GLVs are too volatile to enter the particle phase, it is therefore somehow convincing to get less total number concentration from ozonolysis of GLVs. Comparatively higher particle number concentration was obtained in ozonolysis of cis-3-hexanol when compared to ozonolysis of 3-hexenyl acetate. The differences between these compounds on particle formation could possibly be explained interims of their reaction rate with ozone. When compared, acetates found to have higher reaction rate with ozone than alcohols. It was also observed that the total number concentration found to be decreasing over time shortly after showing an increase in the very beginning of the experiments (for the first 1520min). This sounds logical. Particle coagulation, deposition process and condensation taking place inside the chamber resulted in decrease of the particle concentration and increase of particle size (for instance, see figures 9, 10 and 11 and table 2). Generally, in this study, particle formation rate is found to be higher than the particle formation rates observed in ambient air, which is found to vary in between 0.01–10 cm−3 s−1 (Kulmala et al., 2004). The lower range of the growth rate obtained in our experiment matches to the typical the growth rates of particles formed in atmosphere with the maximum observed growth rate being around 20nmh−1 (Kulmala et al., 2004). Table (3) summarizes literature values for particle number concentration and growth rate values observed in different locations across the globe. 27 Table 3: Summary of literature values showing particle number concentration and growth rate observed at different locations across the globe (Source: Sarangi et al., 2013, p.8). Location Idaho Hill, Corolado Particle size range (nm) Considered nucleation mode size range (nm) Average number concentration (particles/cm3 Average growth rate (nm/hr) References 15–500 3-20 10000 1.6 weber et al., 1997 Rural Ontario, Canada 11–457 10–43 20000 4.2 Verheggen Northern Finland 7-500 7-15 870 2.9 Komppula et al., Rural continental site 3-800 3-20 5000 2.6 Birmili et al., 2003 Po Valley, Italy 3-600 3-20 1200 7 Hamed et al., 2007 Hyytiälä, Finland 3-500 <25 n/a 3 Dal Maso et al., and Mozurkewich, 2002 2003 in Southern Germany 2007 Tokyo, Japan 5-200 n/a 1000 8-17 Mochida et al., 2008 Antarctic 3-1000 3-25 374 1.3 Asmi et al., 2010 Toronto, Cananda 3-100 14–25 105000 6.7 Jeong et al.,2010 Mexico city 10–478 10–15 21000 11.6 Kalafut-Pettibone Beijing, China 12–550 12–25 1000 2.43–13.9 Zhang et al., 2013 Brisbane, Australia 4-110 4-30 560 4.6 Chenung et al., et al., 2010 2011 Shanghai, China 10–500 10–20 13000 4.38 Du et al., 2012 Marikana, South 10–840 12–20 10000 8 Hirsikko et al., Africa 2012 Atlanata, USA 3-500 1-3 1000–10000000 5.5-7-6 Kuang et al., 2012 Wakayama Forest 14–710 14–30 11000 9.2 Han et al., 2013 9-425 9-25 37200 15.4 Sarangi et al., 2013 Research station, Japan National Physical Laboratory NPL, New Delhi 28 The main explanation for the disparity between formation rate and growth rates found in our study and that observed in ambient air could be the difference in concentration of species. Higher concentration of O3, GLVs and MTs has been used in our chamber study than actual atmospheric concentration of the compounds. The other reason for the disparity could be due to differences in actual experimental conditions (e.g., residence times, fluctuations in ozone concentration, fluctuation in RH inside the chamber). 4.2 SOA mass concentration and yield analysis In this section we present the yield of particle mass in secondary organic aerosol (SOA) obtained formed from ozonolysis the GLVs and/or MT in our chamber study. As mentioned in section 3.3, aerosol yields can be determined from progressive changes in VOC concentration and in aerosol mass concentration during the chamber experiment. The yield determination was based on the result obtained from two independent instruments namely the SMPS for size distribution measurement and the PTR for the measurement of concentration. The mass distribution is obtained in the way that we first obtained the size distribution measurement from SMPS data and then we converted the size distribution measurement to the mass distribution measurement assuming the particle density to be 1gcm-3. We are aware that there might be some error on our result as the density of particle could also be a bit more than 1gcm-3. Therefore, we took this into account while analyzing the result. During the second injection period, the concentration of GLVs was increased almost twice (varying between 80-82ppb). As can be clearly seen from the table (4), for all experiments, the mass of SOA particles produced after injection of more VOCs for second time has significantly increased. The maximum mass produced from ozonolysis of α-pinene was about 39gm-3 and 101gm-3 during first and second addition of VOCs respectively. The maximum mass produced after mixing α-pinene with GLV mixture was about 38gm-3 and 53gm-3 during first and second injection respectively. Overall, SOA mass from ozonolysis of GLVs and MTs increased significantly with increasing concentration. And this implies that the concentration of compounds can significantly affect the particle formation and growth in atmosphere. Injection of TME (following VOCs for second time) has resulted in more particle formation from ozonolysis of GLVs and thus increasing mass of the SOA particles. Table (4) shows that for all of the experiments, more SOA particles mass was produced after TME injection. This means our study supports the role of OH in particle formation process. Injection of TME into reaction chamber increased SOA mass production from GLVs, because TME produced OH radicals 29 which would soon react with GLVs producing more SOA. And this is the main reason why injection TME increased the potential of GLVs to produce more SOA particles. Similar finding was also reported by Atkinson et al. (1995). They suggested that GLVs are highly reactive towards hydroxyl radicals and thus producing more SOA particles. Ozonolysis of pure α-pinene and MT-mix produced more SOA mass when compared to SOA mass produced in ozonolysis of mixture of α-pinene with GLVs or MTs with GLVs. For example, the maximum SOA mass produced during ozonolysis of α-pinene alone was about 104gm-3 while the mass SOA produced when monoterpens mixed with the GLVs was about 51 gm-3. So this means there is a decrease in SOA mass when MT is mixed with GLVs than when MT is ozonolysed alone. This implies MTs plays a constitutive role during SOA formation process while GLVs have a suppressing effect on SOA particle formation. On other hand, SOA particle mass concentration slightly increases with time early in the experiments, but then it starts decreasing gradually with time. Losses of particles to the walls of chambers are the main reason for decrease of particle concentration over time. We had also analyzed the yields for each of the experiment (see table 4). Our yield calculation method was basically similar to what has been used by Mentel et al. (2013). They used the VOC consumptions as sum of the individual VOCs when two are more compounds are reacting in the chamber. To determine the yield, we obtained the maximum change in SOA particles mass (∆M tot (µgm-3)) before and after injection of compounds into chamber and then divided by the change in VOC concentration due to consumption (ΔVOC) concentration. The change in VOC consumption was obtained by taking the difference between the maximum VOC consumption and minimum VOC consumption from VOCtime plot. Refer to figures (8, 9, 10, and 11) to see change in VOC concentration over time before and after addition of the GLVs and MTs in to reaction chamber. It was hardly possible to determine the yield from ozonolysis of trans-2-hexenal as in this day we did not observe any significant particle formation and thus the yield calculation was excluded. The yields calculated from ozonolysis of cis3-hexenol and 3-hexynyl acetate were also comparatively low (less than 0.5). Convincingly, ozonolysis of MTs has resulted in higher yield. But during ozonolysis of MT-mix with GLVs, SOA mass yield is found to be decreased. This is because, in ozonolysis of GLVs, the reaction products can be partitioning to gaseous parts decreasing the particles formation and thus the mass of SOA and hence low yield of GLVs. Table (4) shows the summery of the analysis of VOC consumption, ozone conc. change over time, ΔM tot max and the yields obtained during ozonolysis. Table 4: Analysis of VOC consumption, ozone conc. change over time, ΔM tot max and SOA yields 30 Reagents Exp. days MT GLV ΔM tot ΔM tot max max after after inj. one inj. two -3 (µgm ) (µgm-3) ΔM tot max after TME (µgm-3) ΔVOC after inj. one (µgm-3) ΔVOC after inj. two (µgm3 ) Ozon Ozone Yield e conc. one conc. at inj. at inj. (inj.one one two ) (ppb) (ppb) Yield two (inj. two) 7.5.2014 No trans-2hexenal N/A N/A N/A N/A N/A 44 42 N/A N/A 8.5.2014 No cis-3hexenol 0.05 0.26 No inj. 54.5 105 219 195 0.09 0.25 9.5.2014 No trans-2hexenal 0.04 0.13 No inj. 117 256 204 182 0.03 0.05 12.5.201 α4 pinene No inj. 39.4 101 104 281 291 212 185 14 19 13.5.201 α4 pinene trans-2hexenal 30 37.6 48.7 247 128 201 177 12 6.3 14.5.201 α4 pinene cis-3hexenol 44 55 51 1889 305 201 155 2 2.4 15.5.201 α4 pinene 3hexynyl acetate 36.5 44.8 50.5 509 319 210 167 7.2 2 16.5.201 α4 pinene GLV mix 38 38 54 726 272 223 190 5 3.5 19.5.201 MT4 mix No inj. 33.5 70 89 197 136 210 127 17 25.7 20.5.201 MT4 mix trans-2hexenal 15 20 34 135 148 209 199 11 3 21.5.201 MT4 mix cis-3hexenol 19 21 32 343 275 210 178 5.5 1 29.5 30 36.7 220 337 225 185 13 0.2 23 27 32.5 178 272 215 189 13 0.9 22.5.201 MT4 mix 23.5.201 MT4 mix 3hexynyl acetate GLVmix Yield has significantly increased after second injection of VOCs (see table 4). One of the reasons for increase of yield after second injection is because of higher VOC concentration. More VOC concentration in the chamber means more possibility to produce SOA mass (as far as VOCs are available in reaction chamber, the reaction would continue producing more SOA mass) and thus the yield increases. Moreover, it is possible to have some seed particles left in the chamber after addition of the first one, and this could also increase the yield. 31 Previously, few mass yield studies have been reported from chamber studies obtained for SOA particles generated from oxidation of BVOC of real plants. For example, Mentel et al. (2009) reported an incremental mass yields of SOA from OH/O3 initiated pine/spruce emissions. The mass yields obtained in their study were found to be 9%, 8% and 4% for α-pinene, pine and spruce SOA, respectively. Their reported values are slightly lower than the value we found in our study. We suspect this difference in mass yields could be due to differences in experimental conditions (e.g., different reaction chamber system, reactant and ozone concentration and humidity). 4.3 Growth Factor (GF) values In H-TDMA experiments, we measured the diameter-based hygroscopic GF of the SOA particles as function of time. Therefore, in this section, we report the GF values obtained from H-TDMA measurements. Among other figures located on the appendix (A2.1-A2.9), figures (1411, 1512, and 1613) and table (5) (6) shows growth factor data measurement obtained from H-TDMA measurements. All SOA particles generated in this study were found to be less hygroscopic (or showed smaller water uptake property when compared to that of typical inorganic aerosol substances (such as (NH4)2SO4)). The maximum GF value obtained in the measurement is 1.1305 which is measured at dry diameter of 50nm. We found GF values in between 1.01–1.13 for SOA particles formed from ozonolysis of both GLVs and monoterpenes. It was also observed that for each precursor, the GF values computed from different dry diameters agree with each other (i.e. there is no such a significant difference among the measured GF values). Overall, this result suggests that the SOA obtained from ozonolysis of monoterpens and GLVs has very low hygroscopicity showing very little water uptake with growth factor between 1.01-1.03. All the GFs values from monoterpenes and GLVs are contained within narrow range of GF values (in between 1.01-1.03). 32 Table 5: Summary of the mean values of growth factor (GF) values for some selected dry particle sizes Exp.days MT 07-05-2014 GLVs GF GF GF GF (Dp=30nm) (Dp=50nm) (Dp=100nm) (Dp=150nm) trans-2hexenal n/a n/a n/a n/a 08-05-2014 ----------- cis-3hexenol 1.13 1.13 n/a n/a 09-05-2014 ----------- 3-hexynyl acetate 1.06 1.05 1.03 n/a 12-05-2014 α-pinene ------------- 1.06 1.07 1.07 n/a 13-05-2014 α-pinene trans-2hexenal 1.06 1.06 1.05 1.05 14-05-2014 α-pinene cis-3hexenol 1.06 1.06 1.05 1.04 15-05-2014 α-pinene 3-hexynyl acetate 1.04 1.05 1.04 1.04 16-05-2014 α-pinene GLV-mix 1.05 1.06 1.05 1.05 19-05-2014 MT-mix ---------- 1.05 1.04 1.03 1.02 20-05-2014 MT-mix trans-2hexenal 1.07 1.06 1.05 1.04 21-05-2014 MT-mix cis-3hexenol 1.06 1.06 1.05 1.04 22-05-2014 MT-mix 3-hexynyl acetate 1.05 1.04 1.03 1.02 23-05-2014 MT-mix GLV-mix 1.06 1.05 1.04 1.03 33 Figure 11: Plot of growth factor as function of time for ozonolysis of trans-2-hexenol 34 Figure 12: Plot of growth factor as function of time for ozonolysis of α-pinene 35 Figure 13: Plot of growth factor as function of time for ozonolysis of MT-mix and GLV-mix The GF range obtained in our measurement is in a good agreement with previously reported values for some BSOA. For example, Virkkula et al. (1999) reported GF to be 1.1 at 84 %RH for products of α-pinene and limonene which were measured at 90%RH. Similarly, Varakutbangkul et al. (2006) also measured the GFs values (at 85%RH) and reported it to be in range between 1.09-1.16 for ozonolysis products of cycloalkenes, 1.06-1.1 for photooxidized monoterpenes and oxygenated terpenes and 1.01- 1.04 for photooxidized sesquiterpenes. 36 Chapter 5: CONCLUSIONS AND RECOMMENDATIONS 5.1 Conclusions We have studied the secondary organic aerosol formation from ozonolysis of green leaf volatiles and (monoterpenes) by using chamber experiments performed in humid conditions (50%RH). New particle formation generated from ozonolysis were characterized. Accordingly, aerosol formation, aerosol condensational growth, aerosol mass yield and hygroscopicity were measured and investigated by using instruments such as SMPS, PTR-MS and H-TDMA. SOA particle formation rate in our experiment was higher than the particle formation rates observed in ambient air, which is found to vary in between 0.01–10 cm−3 s−1. The main reason for this disparity could be because of higher concentration of GLVs, MTs and O3 used in our reaction than the actual concentration of ambient air. Our study also showed that VOCs emitted from green leaf plants less effectively involved in particle formation than from monoterpenes. We investigated that there is a decrease in SOA mass during ozonolysis of the mixture of MT and GLVs than when MT is ozonolysed alone. GLVs have potential to decrease the SOA particle number concentration and thus the particle mass. So this indicates that MT plays a constitutive role during SOA formation process while GLVs has a suppressing effect on particle formation event. The SOA yields were: 14% for ozonolysis of α-pinene, 17% for ozonolysis of MT-mix, 12.3 % for mixture of α-pinene and trans-2-hexenal, 2.33 % for mixture of α-pinene and cis -3- hexen-1-ol, 7.2% for mixture of α-pinene and cis -3-hexenyl acetate and 13.2 % for the mixture MT and GLVs. The SOA mass yield from ozonolysis of pure GLVs is much less than the above reported values. Moreover, the yield showed a decrease when MTs is mixed with GLVs. We have also investigated that more concentration of VOCs in chamber resulted in higher SOA mass yield values. SOA mass yields obtained in our study are higher than previously reported studies from chamber studies of real plant BVOC oxidation. We suspect this difference in mass yields could be due to differences in experimental conditions (e.g., different reaction chamber system, reactant and ozone concentration and humidity). We have also studied hygroscopic growth of SOA particles and the result suggests that SOA particles have very low hygroscopicity showing low water uptake property with growth factor value in between 1.01-1.03. 37 5.2 Recommendation for further research In this study only three GLV compounds have been studied, but there are a number of other GLV species emitted into the atmosphere from vegetation showing that the SOA potential of green leaf volatiles may be considerably higher than what our results indicate here. Therefore, it is important to have further work on emission fluxes, simulation chamber studies, field measurements and modelling so as to fully evaluate the significance of GLVs to the SOA budget in atmosphere. We still suspect that there could be a visible link between green leaf volatiles and new aerosol particle formation. Therefore, further research and measurements are necessary in order to get more reliable information in this regard. 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APPENDIXES Appendix 1: Figure (A1.1-A.8): Contour plot of aerosol particle number size distributions, total aerosol particle number and mass concentration, O3 concentrations and VOC concentration during ozonolysis experiments. 43 Fig.A1.1: Particle formation from ozonolysis of α-pinene and trans-2-hexenal 44 Fig.A1.2: Particle formation from ozonolysis of α-pinene and cis-3-Hexanol 45 Fig.A1.3: Particle formation from ozonolysis of α-pinene and 3-hexynyl acetate 46 Fig.A1.4: Particle formation from ozonolysis of α-pinene and GLV-mix 47 Fig.A1.05: Particle formation from ozonolysis of MT-mix 48 Fig.A1.6: Particle formation from ozonolysis of MT-mix and trans-2-hexenal 49 Fig.A1.7: Particle formation from ozonolysis of MT-mix and cis-3-hexanol 50 Fig.A1.8: Particle formation from ozonolysis of MT-mix and 3-hexynyl acetate 51 Appendix 2: Figures A2.1-A2.9 shows the hygroscopic growth factor as function of time of ozonolysis experiment Fig. A 2.1: A graph of growth factor as function of time for ozonolysis of cis-3-hexanol 52 Fig. A 2.2: A graph of growth factor as function of time for ozonolysis of mix of α-pinene and trans-2-hexenal 53 Fig. A 2.3: A graph of growth factor as function of time for ozonolysis of mix of α-pinene and cis3-hexanol 54 Fig. A 2.4: A graph of growth factor as function of time for ozonolysis of mix of α-pinene and 3hexynyl acetate 55 Fig. A 2.5: A graph of growth factor as function of time for ozonolysis of mix of MT-mix and GLV-mix 56 Fig. A 2.6: A graph of growth factor as function of time for ozonolysis of mix of MT-mix 57 Fig. A 2.7: A graph of growth factor as function of time for ozonolysis of mix of MT-mix and trans2-hexenal 58 Fig. A 2.8: A graph of growth factor as function of time for ozonolysis of mix of MT-mix and Cis3-hexanol 59 Fig. A 2.9: A graph of growth factor as function of time for ozonolysis of mix of MT-mix and 3hexynyl acetate 60 Appendix 3: Summary of work plan Activity Total amount of Dates days Finding and reading literatures and preparing thesis Four weeks 1/04/2014-31/04/2014 research plan Designing the experiment and practicing how to use 5 days 01/05/2014-5/05/2014 the materials Running the experiments and collecting and Four weeks 06/05/2014-31/05/2014 organizing data Analyzing the data Eight weeks 01/06/2014-30/072014 Writing the report Eight Weeks 01/08/2014-30/09/2014 Submission of the first draft, Rewriting and Four weeks 01/10/2014-30/10/2014 Thorough proof-reading MSc thesis defense and submission of the final work Nov 2014 Nov 2014
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