Interactive comment on “ A Marine Aerosol Reference Tank system as a breaking wave analogue ” by M . D . Stokes

Additional data and text has been added to the revised manuscript, to address this and the comments from Reviewer 2 regarding foam persistence. The 20 cm wide by approximately 1 cm thick sheet (in free fall) creates a bubble plume that penetrates about 25 cm after a 10 cm drop (all these dimensions can be varied in the tank). Above the rising bubble plume, a surface patch of foam is produced, with time-evolving characteristics depending on the water temperature, salinity and presence of surfactants in the tank. By using filtered seawater in a 3 s flowing sheet followed by an 8 s pause to allow C4088


Introduction
Sea Spray Aerosols (SSA) are critically important components in global biogeochemical cycles (e.g.Solomon et al., 2007) and important modifiers of atmospheric radiative budgets because they are generated over a large portion of the Earth's surface and form a large fraction of aerosol particulates present in the atmosphere (e.g.Lewis and Schwartz, 2004).Marine aerosols are generated primarily by processes associated with the formation of bubble plumes and foams generated by the actions of breaking surface waves.Breaking waves themselves play an important role in many additional processes at the air-sea interface including mixing, current formation, heat and momentum flux, and the entrained bubbles enhance gas transport, scavenge biological surfactants, and generate ambient noise in addition to creating aerosol particles.
Oceanic whitecaps (the high optical albedo footprint of a breaking surface wave) typically form once wind speeds greater than approximately 3 m s −1 blow over a sea surface of appropriate fetch.Breaking itself includes the impaction of the overturning wave crest with the sea surface and subsequent entrainment and fragmentation of air into a plume of bubbles.The plume evolves over a timescale of seconds to a few tens of seconds due to buoyancy and turbulent flow forces acting on the entrained bubbles.
The air/water mixture of the breaking wave crest and the bubbles that reach the sea Figures surface after breaking form the high albedo patch characteristic of a whitecap.Surface bubbles and the dense aggregations of bubbles that create surface foams, are the primary source of marine aerosols as the bubbles rupture and produce a spray of jet and fluid film droplets that are ejected into the atmosphere.
The detailed investigations by Sellegri et al. (2006) and Fuentes et al. (2010) have shown that the best method for the laboratory generation of proxy marine aerosols is by creating a bubble plume from a plunging jet of water.The method of generation used had a strong influence over the chemical and physical properties of the aerosols produced in including variation in organic enrichment, formation of condensation nuclei and variation in hygroscopicity (Fuentes et al., 2010) and bubbles generated by the plunging jet more closely approximated those from oceanic measurements.The plunging jet apparatus used by Fuentes et al. (2010) used a relatively small volume of water (6 L) in an 11 L tank filled to a depth of 11 cm and their investigations suggested that in order to better duplicate the characteristics of oceanic plumes (including bubble lifetime), the dimensions of current laboratory systems would have to be enlarged.
Here we show the fabrication of a Marine Aerosol Reference Tank (MART) system that can accurately reproduce the bubble plumes and marine aerosols characteristic of an oceanic whitecap.By using an intermittent plunging sheet of water in a larger (210 L) Introduction

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Full tank bubble plumes are formed that mimic the size distribution, including critical bubbles larger than the Hinze scale (the transition point between bubbles stabilized by surface tension and bubbles subject to fragmentation by turbulence at approximately 1 mm), and have a temporal evolution similar to plumes measured in the ocean and in large laboratory wave tanks.Because the production of the bubbles can be continuously monitored acoustically, and the physical and chemical conditions of the MART system can be carefully controlled, the resulting aerosols generated by these bubble plumes are not only very similar to natural marine aerosols, they can also be duplicated in replicate experiments.

Whitecap foam and bubble size distributions
The two primary production mechanisms of sea spray aerosols at moderate wind speeds are the disintegration of the thin fluid films associated with whitecap foam (film drops) and the break up of the jet of water formed at the base of a bubble shortly after the rupture of its film (jet drops).Both of these mechanisms are known to be sensitive to bubble size.It follows that an essential requirement of any laboratory system designed to produce nascent SSA is the reproduction of the numbers and sizes of bubbles entrained by breaking waves in the open ocean.Few bubble size distributions from natural breaking waves have been acquired because of the difficulty of making measurements in stormy conditions and other natural hazards (Herrero, 1985;Melville, 1996;de Leeuw and Cohen, 2002;Stokes et al., 2002).However, some oceanic measurements are available in addition to a number of laboratory studies (e.g.Monahan and Zeitlow, 1969;Cipiriano and Blanchard, 1981;Bezzabotnov et al., 1986;Lamarre and Melville, 1994;Loewen et al., 1995;Leighton et al., 1996;Deane and Stokes, 2002;de Leeuw and Cohen, 2002;de Leeuw and Leifer, 2002;Leifer andde Leeuw, 2002, 2006;Stokes et al., 2002).Measurements of bubble size distributions within whitecaps in two oceanic studies and a laboratory study are shown in Fig. 1.It is now known that there is a scale dependence to the bubble creation physics, differentiated by a length scale known as the Hinze scale (Deane and Stokes, 2002).The Hinze scale (a H ) defines the radius of a bubble for which surface tension forces, which tend to keep bubbles spherical, are balanced by distorting forces associated with fluid turbulence.This scale is of the order of 1 mm in spilling and breaking waves.Bubbles smaller than the Hinze scale are stabilized to fragmentation by fluid turbulence whereas bubbles larger than this scale are subject to a turbulent fragmentation cascade.
The power law dependence of the bubble size distribution as a function of bubble radius is also different for bubbles smaller and larger than the Hinze scale.Smaller bubbles have a somewhat variable power law scaling, a −n with n taking values between approximately 1 to 2. This variability can be seen in measured distribution slopes for bubbles smaller than a H in Fig. 1.The physics of bubble fragmentation and bubble degassing drives a steeper power law dependence for bubbles larger than the Hinze scale with n taking values between approximately 3 to 4 (Fig. 1).The two relevant points here are: (1) breaking waves can produce large bubbles, greater than 1 mm radius and up to 4 mm radius (Bowyer, 2001), and (2) the power law scaling of the generation of these bubbles is controlled by fluid turbulence within the whitecap and differentiated by the Hinze scale.In order to accurately reproduce nascent SSA, the laboratory bubble generation mechanism needs to produce bubbles larger than the Hinze scale and reproduce the power law dependence those bubbles acquire through fragmentation in fluid turbulence.
3 The Marine Aerosol Reference Tank (MART) The MART system was constructed to closely mimic the bubble plume, foam, and aerosol generating mechanisms active during oceanic wave breaking and to provide a portable, controllable environment in which to explore and sample these processes.The primary design of the system includes a flow-controlled closed-loop seawater (or freshwater) circulation system that draws from the tank bottom, a tank-top spillway or waterfall to produce a plunging sheet that impacts the water surface within the tank Introduction

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Full to produce a bubble plume, and an air-tight headspace for controlled aerosol sampling while the system is operating.Instrumentation (flow meter, acoustic monitoring) is incorporated into the design to insure plume generation consistency during long experimental runs and repeatability over separate experimental setups.By varying the temperature of the tank contents, the water chemistry and the characteristics of the plunging sheet (volume, angle and distance of drop, timing of the intermittency) a wide range of experimental conditions can be realized.
The MART system (Fig. 2) was fabricated using components that are readily available and constructed of stainless steel, plexiglass and silicone wherever possible to minimize chemical contaminates and facilitate cleaning.The tank was modified from a 210 L plexiglass aquarium (AquaClear) that was drilled to accept an o-ring sealed, 20 mm thick plexiglass lid to provide airtight integrity.All fittings were attached to the tank through threaded bulkheads made from 25 mm thick plexiglass plates, tapped to accept standard stainless steel pipe fittings (NPT-thread).In order to minimize flow resistance and maximize pump efficiency, the circulation system was designed with short pipe lengths and large internal diameter (20-25 mm) fittings.Pumping was provided by a 1/3 HP centrifugal pump (AMT Pumps) capable of pumping more than 70 L min −1 and powered by 110 V electric motor.A valved shunt in the circulation loop allows the regulation of the return flow to the tank between approximately 15 L min −1 and the maximum pumping rate, and is monitored using an in-line flow meter (GPI products TM-15).The intermittency of the tank return flow is regulated using a solenoid valve (Parker Fluid Controls J5011) controlled by two time-delay relays (Macromatic TR53122) adjustable between 0 and 10 s.Separate ports are available for sampling both the atmospheric headspace and subsurface water in the tank.All electric motor controls and the solenoid timer relays are contained in a water resistant box for protection.At present, the MART system is mounted to a wheeled aluminum chassis for easy portability.
Water that enters the tank is formed into a plunging sheet that impacts the water surface to mimic the plunging jet of water from a breaking wave crest (Fig. 3).The Introduction

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Full water exiting the pump system is channeled through an o-ring sealed plexiglass tube approximately 8 cm internal diameter that contains a secondary internal diffuser (3 cm diameter tube with holes spaced at regular 2 cm distances along its length) to evenly distribute the water within.Water exits this nested tubing through an approximately 6 mm wide × 20 cm long slot in the outer tube and plunges as a sheet into the tank.In the configuration described here, the water level within the tank was kept constant to provide an approximately 10 cm drop between the plunging sheet and surface, producing a bubble plume penetrating about 25 cm beneath the surface and bubbles in a wide range of sizes up to about 1 cm in diameter.The length of the slot can be varied depending on the experimental requirements as can the number of slots in the spillway.
For example, a single slot was used to examine plume and foam patch characteristics, and a two slot configuration (with the slots at 180 • along the length of the spillway) has been used to maximize the generation of aerosols during a plunging event.
Before experimentation the MART system is cleaned to minimize contamination.The internal tank surfaces are scrubbed with 100 % isopropanol and then the entire system is filled and the pump and spillway circulated with a 10 % isopropanol/deionized water solution for approximately 30 min.After circulation the tank is drained and then rinsed with deionized water, and the system again circulated.Lastly, the system is flushed with filtered freshwater (or seawater) and circulated while the tank water level is held constant by balancing the water input and tank drain flow rates.The MART system is considered clean when measurements of surface tension from tank water samples are the same as those from the filtered water supply used for experimentation (approximately 72 mN m −1 measured using the Wilhemy plate method with a Kr üss K3 tensiometer.)Although it has been possible to sufficiently clean the MART system with its mix of different construction materials (primarily plexiglass and stainless steel), the design is simple enough that an entire system could potentially be fabricated almost entirely of stainless steel and glass should more aggressive cleaning be required.Introduction

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Bubble size distribution measurements
To examine the utility of the MART system as an oceanic bubble plume proxy, the size distributions of bubbles within the tank plumes were compared to those produced by sintered glass filters as well as to oceanic and laboratory wave channel distributions.The glass filters were set at a depth of ∼ 25 cm (filter surface to water surface) and dry nitrogen gas (0.5 L min −1 ) was pumped through four filters, two 90 mm diameter type E filters and two 25 mm diameter type A filters, similar to the setup of Keene et al. (2007).
The plunging sheet peak flow rate was approximately 1 L min −1 , falling through a height of approximately 10 cm, and modulated with on/off times of approximately 4 s on and 10 s off.
The sintered glass filter and plunging sheet bubble size distributions were obtained utilizing methods described previously by Deane and Stokes (2002).In brief, bubble plumes were imaged a few centimeters from the side of the tank using a high-resolution digital camera (Nikon).The distribution of bubble sizes was then obtained through computer-aided analysis of the images.The cross-sectional area of individual bubbles within a selected image were determined and then transformed into equivalent spherical radii.This data combined with an estimate of the imaging volume formed the basis of the bubble size distributions presented in Fig. 4.
The reference distribution for a laboratory plunging breaking wave from Deane and Stokes (2002) is in absolute units of bubbles m −3 µm −1 radius increment, which is standard for the oceanographic literature.The absolute level of the distributions for sintered glass filters and plunging water were variable, depending on air flow, plunging sheet height and roughness, among other factors.To facilitate comparison with the breaking wave, the bubble size distributions for the sintered glass filters and plunging waterfall were first converted to probability density functions (PDFs) and then scaled by 5.6×10 6 .
The scaling factor was determined to be the value which brought the plunging waterfall and breaking wave distributions into agreement at a bubble radius of < 1 mm.Introduction

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Full Sampled particles are directed past a 0.058 cm impactor to remove particles too large for analysis and into the DMA column, which separates particles by electrical mobility.The range of particle sizes which can be analyzed in this way is dependent on the aerosol and sheath flow rates, which were set at 0.4 and 4.0 L min −1 , respectively, which corresponds to particle diameters of 10-600 nm.Particles selected in the DMA are injected into a condensation particle counter (TSI Model 3010), which counts the particles over a range of size bins.
The APS (TSI Model 3321) determines the aerodynamic diameter (d a ) of particles in the 0.542 to 20 µm range by measuring particle time-of-flight.Particles were sampled at 5.0 L min −1 (1.0 and 4.0 L min −1 , aerosol and sheath flow rates, respectively).To determine d a , particles enter the inlet of the APS and pass between two separate paths of a CW laser split with a beamsplitter.For both the SMPS and APS analysis, particles passed through silica gel diffusion driers, where they were dried to an RH of 15 ± 10 %.The d m and d a size distributions recorded were merged to obtain a geometric physical diameter (d p ) size distribution.
For the purposes of merging, particles sized by the SMPS were assumed to be of a spherical geometry, which allows for the relation: Particles sized by the APS were assigned an effective density, ρ eff , of 1.8 g cm −3 , a value determined experimentally, which allows for conversion based on the relation: Introduction

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Full (2) with ρ equal to unit density (i.e. 1 g cm −3 ).Both instruments had their resolution set to 32 bins per decade for consistency in merging.The SMPS tends to undercount particles at the high end of the distribution due to the cut-off from the particle impactor, while the APS can undercount particles at the low end due to poor scattering efficiency of the smallest particles.As a result, particle bins in the overlapping size region of the two methods were subsequently removed, excluding the largest and smallest bins of the SMPS and APS, respectively (Fig. 5).
During MART operation, carrier gas (either N 2 or synthetic air) is supplied to the sealed tank at flow rates ranging between 1-10 slpm depending on instrument sampling requirements.The carrier gas flow, combined with particle deposition within the tank determine the average lifetime of a particle in the system prior to sampling.The e-folding time with respect to mixing is set by the headspace volume (90 L) and the carrier gas flow rate.For the three flow rates studied here (1, 3, and 6 slpm) the average particle lifetime with respect to mixing are 90, 30, and 15 min, respectively.To assess deposition within the tank, we arrest plunging and particle production and monitor the decay in the size dependent number concentration.Size dependent decay rates are shown in Fig. 6 as a function of carrier gas flow.For the decay analysis, we use an Ultra High Sensitivity Aerosol Spectrometer (UHSAS) operating at 1 Hz for the submicron size distributions (Cai, 2008).The deviation in the decay from that determined from mixing alone is a low-bound on particle deposition within the tank.Actual deposition rates are likely faster when the plunging waterfall is on.As shown in Fig. 6, particle deposition is strongly size dependent, where the observed particle lifetimes span between 2 and 63 min for a carrier gas flow rate of 1 slpm.Introduction

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Full Particle lifetime with respect to deposition (τ DEP ) is calculated from the observed lifetime (τ OBS ) and that expected from mixing (τ MIX ) via Eq.( 3) and shown in Fig. 7b.
As expected, the in-tank deposition is strongly dependent on particle size, where particles with diameters greater than 2 µm have τ DEP as small as 2 min, while particles in the size window of 60-200 nm display τ DEP that is 2-3 times τ MIX (τ DEP = 113-209 min).Further, τ DEP is dependent on the carrier gas flow rate, with increased deposition rates at higher carrier gas flows.As a result, bias in the measured size distribution is expected for particles where τ DEP is significantly smaller than τ MIX (e.g.d p > 2 µm; τ DEP = 1.5 min and τ MIX = 90 min for 1 slpm carrier gas flow), highlighting the importance of running proper aerosol dynamic simulations when determining size distributions.Total number, surface area, and mass concentrations are dependent on the choice of carrier gas flow as shown in Table 1.Given fast in-tank deposition of larger particles, enhancements in surface area and mass (carried by the larger particles) are less pronounced at low carrier gas flow rates than would be expected from the observed increase in particle number.

Monitoring performance characteristics
The air entrained by the plunging waterfall was monitored throughout the experiment by analyzing the underwater noise radiated by newly-formed bubbles within the plumes (Deane and Stokes, 2010).The acoustic signature of the plunging jet and forming bubble plume is characteristic of particular pump and flow conditions and by monitoring the sound production we can ensure that these flow conditions are repeatable over time.The acoustic measurements were conducted using a hydrophone (ITC 1089d) placed a few centimeters from the bubble plumes and analyzed with a Stanford Research Systems SR785 Dynamic Signal Analyzer.Acoustic reverberation within the tank makes a quantitative analysis of the noise problematic, however, by keeping the Introduction

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Full hydrophone position relative to the plume fixed and generating a reference acoustic spectrum at the beginning of an experimental run, it is possible to detect changes in air entrainment conditions over time.In addition to the acoustic monitoring, the flow rate of water supplied to the spillway is measured using a digital flow meter downstream of the circulation pump and any variation in flow can be adjusted using the shunt flow valve.
In Fig. 8, the acoustic spectrum recorded at three different plunging sheet flow rates (0.6, 0.75 and 0.95 l s −1 ), each at three different times during an experimental session is shown.Even though the sound being generated by each plunging sheet is from a seemingly random ensemble of ringing bubbles in a turbulent flow field, the acoustic power in certain frequency bands (e.g. 4 kHz) is relatively conserved at each flow rate and set of tank conditions as shown by the clustering of the red, green and blue lines in Fig. 8.By monitoring the acoustic spectrum for large variations, the MART system can be configured to replicate bubble plume production in separate experiments (i.e. by adjusting the flow rate, height of the plunging sheet, angle of the spillway, duty cycle of the solenoid valves) and thus consistently replicate the aerosol source.And by regularly monitoring the acoustic spectrum during a experimental session, any drift in production mechanism attributable to changes in the bubble plume can be noted, adjusted or compensated for.

Comparison of MART to other generation methods
As noted by Sellegri et al. (2006) and Fuentes et al. (2010), a plunging water jet best replicates the bubble plumes generated by an oceanic whitecap.Comparison of the bubble plume formed by the MART system to those generated by air flow through sintered glass filters and to those formed in oceanic waves and within a large laboratory wave channel (Figs. 1, 4) illustrates that a plunging sheet of water forms a broader spectrum of bubble sizes than the sintered glass filters tested, including critical bubbles larger than about 1 mm in radius.The slopes of the bubble density size spectrum in the MART plumes are very similar to the slopes of oceanic and laboratory breaking waves Introduction

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Full at sizes smaller and larger than the Hinze scale (a H ). The bubble plumes generated by the sintered filters have a much narrower size spectrum and tend not to include bubbles larger than about 800 µm radius.By using a much larger volume tank than that used by Fuentes et al. (2010), the bubble plumes generated by the plunging sheet can penetrate 20 to 30 cm beneath the water surface which is similar to the penetration depths of plumes generated by spilling breakers in the lab and ocean (Deane and Stokes, 2002;Melville, 1996).The intermittent cycling of the plunging jet in the MART system allows the bubble plume and resulting surface foam patch (Fig. 3) to evolve over time creating a bubble and aerosol source that is a closer match to the decaying patches of foam produced by whitecaps than that provided by constant, stationary jets.The importance of decaying foams (as opposed to pseudo steady state foams, for which decay rates are matched by bubble entrainment rates) remains an open question, but may be important.For example, the jet drop production mechanism may be somewhat suppressed in steady state foams if they are more than a single bubble layer thick because of the top layer of foam film absorbing jet drop aerosols produced at the air-water interface.Foams allowed to decay even if they are initially three dimensional in structure, will eventually devolve into 2 dimensional rafts of bubbles which will not suppress jet drops.
The particle number distribution measured using the MART system is broader and peaks at a significantly larger diameter as compared with particle number distributions obtained using sintered glass filters (Fig. 5).Though similar to the size distribution obtained by Fuentes et al., it is notable that the particle number distribution obtained using the MART system has less pronounced characteristics of sub-100 nm modes, with the dominant number distribution mode around 200 nm, broadly tailing off to both larger and smaller sizes.This result is consistant with the broad bubble size spectrum and accurate representation of bubble larger that 1 mm that is achieved by MART system.Particle number distributions measured in the MART system are in strong agreement with those previously measured from breaking waves in the Scripps Institution of Oceanography Hydraulics Laboratory (Prather et al., 2012).These measurements

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Full highlight the importance of an accurate representation of bubble formation processes in the creation of sea-spray aerosol in the laboratory.

Conclusions
In order to faithfully reproduce the aerosols created by breaking oceanic waves any surrogate system must mimic the complex two-phase flows, bubble plumes and surface foam patches naturally generated during whitecap formation.These conditions can be replicated in large seawater breaking wave channels, however these facilities are not readily available, and due to their large volume it is extremely difficult to satisfactorily enclose them for high fidelity aerosol sampling and to carefully control the environmental conditions within them.Sintered glass filters (frits) sparged with air in an enclosed tank produce controllable plumes, however the bubbles produced are constrained to a size spectrum that is considerably narrower than the spectrum observed in laboratory and open ocean breaking waves.In order to reproduce the broad spectrum of bubbles from a breaking wave would require injecting air through multiple frits of varying size and varying injection rate, but even then the slopes of the bubble distributions produced would need to reflect the change in slope observed about the Hinze scale in natural distributions.When creating plumes using plunging water, it is important that the falling sheet or jet have the appropriate scale of surface roughness before impacting the water surface in order to create the correct sized voids along the air/water interface (Zhu et al., 2000).
The larger voids in particular are critical for producing the correct plume bubble size distribution that includes bubbles larger than the Hinze scale.Stationary, narrow crosssectional area and high velocity jets may not entrain large bubbles characteristic of whitecaps without the correct scale of disturbances on their surface before impacting the water.
It may be important that any bubble plume creation mechanism provide the correct intermittency in production.Natural plumes and the resulting surface foam patches Introduction

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Full evolve over a time scale of seconds to tens of seconds.Continuous jets impacting the surface at a fixed location create subsurface flow fields unlike breaking events.Continuous sparging of air through frits or air entrainment by continuous jets can also create three dimensional surface foams that do not evolve and dissipate like within natural whitecaps and then can bias physical and chemical attributes of the aerosols created when the bubbles rupture (submitted Science paper).
The resulting particle size distribution generated within the MART system closely resembles that generated from breaking waves within the SIO glass-walled wave channel.Confining the bubble generation to a smaller headspace air volume (< 50 L) as compared to the wave channel, permits a significant increase in particle number concentrations (from 100 to greater than 5000 particles cm −3 , for the wave channel and MART system, respectively).As a result, the MART system enables a wide array of measurements (e.g.size resolved hygroscopicity and heterogeneous reactivity) that are not feasible at the low number concentrations produced in the wave channel.
The MART system provides many benefits for the controlled study of the chemistry and physics of marine bubbles, foam and aerosols.Because the air entrainment processes are monitored, experiments are repeatable even while environmental variables, like the seawater and atmospheric chemistry and the physical forcing mechanisms controlling the plume dynamics are manipulated.Furthermore, the MART provides a standardized, easily fabricated, portable aerosol source for studies across separate labs or for shipboard use while at sea.Introduction

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Full The grey lines show reference power law scalings for bubble distributions.Theoretical considerations lead to an a −10/3 power law scaling for bubbles larger than the Hinze scale (approximately 1 mm).Bubbles smaller than the Hinze scale are more variable in their power law scaling but roughly follow an a −3/2 trend (Deane and Stokes, 2002).Purple squares are Loewen et al. (1995), green, Bezzabotonov et al. (1986) and blue line from Cirpriano and Blanchard (1981).
Discussion Paper | Discussion Paper | Discussion Paper | Discussion Paper | Discussion Paper | Discussion Paper | Discussion Paper | Discussion Paper | Discussion Paper | Discussion Paper | Discussion Paper | Discussion Paper | Discussion Paper | Discussion Paper | Discussion Paper | Screen / Esc Printer-friendly Version Interactive Discussion Discussion Paper | Discussion Paper | Discussion Paper | Discussion Paper | Discussion Paper | Discussion Paper | Discussion Paper | 3.2 Aerosol size distributions and residence time Particle size distributions (PSDs) were determined by a commercially available TSI Scanning Mobility Particle Sizer (SMPS) and Aerodynamic Particle Sizer (APS).The SMPS measures particle mobility diameter (d m ) by scanning voltages through a TSI electrostatic classifier with differential mobility analyzer (DMA) column (Model 3080).
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Fig. 1 .
Fig. 1.Bubble size distribution (density vs. bubble radius) in open ocean and laboratory whitecaps.The grey lines show reference power law scalings for bubble distributions.Theoretical considerations lead to an a −10/3 power law scaling for bubbles larger than the Hinze scale (approximately 1 mm).Bubbles smaller than the Hinze scale are more variable in their power law scaling but roughly follow an a −3/2 trend(Deane and Stokes, 2002).Purple squares areLoewen et al. (1995), green, Bezzabotonov et al. (1986)  and blue line from Cirpriano andBlanchard (1981).

Fig. 2 .Fig. 4 .
Fig. 2. Marine Aerosol Reference Tank (MART).The 210 L plexiglass tank (A) is approximately 1 m in the longest dimension.(B) the internal water distribution assembly is o-ring sealed with central spillway slot.Inside the assembly is a secondary diffuser tube (not visible) for evenly distributing the water along the spillway.(C) Flowmeter.(D) Tank water sampling spigot.(E) 1/3 HP Centrifugal pump.(F) Flow shunt control valve.(G) Timing relay control box.(H) Tank drain and purge valves.(I) Solenoid valve.