Velocity Dependent Passive Sampling for Monitoring of

Oct 15, 2013 - Micropollutants in Dynamic Stormwater Discharges ... through passive sampling may revolutionize the way stormwater discharges are ...
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Velocity dependent passive sampling for monitoring of micropollutants in dynamic stormwater discharges Heidi Birch, Anitha Kumari Sharma, Luca Vezzaro, Hans-Christian Holten Lützhøft, and Peter Steen Mikkelsen Environ. Sci. Technol., Just Accepted Manuscript • DOI: 10.1021/es403129j • Publication Date (Web): 15 Oct 2013 Downloaded from http://pubs.acs.org on October 20, 2013

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Environmental Science & Technology

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Velocity dependent passive sampling for monitoring of

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micropollutants in dynamic stormwater discharges

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Heidi Birch, Anitha K. Sharma, Luca Vezzaro, Hans-Christian H. Lützhøft and Peter S. Mikkelsen*

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Department of Environmental Engineering (DTU Environment), Technical University of Denmark

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(DTU), Miljoevej, Building 113, 2800 Lyngby, Denmark

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*Corresponding author, e-mail [email protected], +45 4525 1600.

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Micropollutant monitoring in stormwater discharges is challenging because of the diversity of sources

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and thus large number of pollutants found in stormwater. This is further complicated by the dynamics in

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runoff flows and the large number of discharge points. Most passive samplers are non-ideal for

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sampling such systems because they sample in a time-integrative manner. This paper reports test of a

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flow-through passive sampler, deployed in stormwater runoff at the outlet of a residential-industrial

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catchment. Momentum from the water velocity during runoff events created flow through the sampler

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resulting in velocity dependent sampling. This approach enables the integrative sampling of stormwater

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runoff during periods of weeks to months while weighting actual runoff events higher than no flow

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periods. Results were comparable to results from volume-proportional samples and results obtained

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from using a dynamic stormwater quality model (DSQM). The paper illustrates how velocity-dependent

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flow-through passive sampling may revolutionize the way stormwater discharges are monitored. It also

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opens the possibility to monitor a larger range of discharge sites over longer time periods instead of

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focusing on single sites and single events, and it shows how this may be combined with DSQMs to

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interpret results and estimate loads over extended time periods.

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INTRODUCTION

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Stormwater runoff from residential and industrial areas contains a wide range of pollutants,1-3 which

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can cause adverse effects in receiving waters and prevent these from obtaining a good chemical status as

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e.g. required by the European Water Framework Directive4 as well as by the US Clean Water Act.5

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However, the concentrations of pollutants in stormwater are variable from site to site and from event to

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event.6 In order to justify the need for treatment at a particular site and to evaluate the selected

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treatment, monitoring of stormwater discharges is important.7 Traditionally, this is achieved by using

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autosamplers in a volume-proportional manner (a fixed volume of sample is collected at a defined

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runoff volume interval) or flow-proportional manner (a flow weighted volume is collected at a defined

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time interval). These campaigns are usually very costly and involve many practical difficulties.8

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Stormwater sampling campaigns are thus often non-ideal, for example by omitting periods with extreme

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weather (where sampling is difficult) or by focusing on spot-sampling or sampling of only the first part

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of events.

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Passive sampling devices (PSDs) have been developed for monitoring of water quality in surface

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waters such as lakes and streams. Most PSDs are based on diffusion of solutes through a membrane or

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diffusion layer to a collecting phase.9 In this way mainly the dissolved fraction (labile or bioavailable)

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will be subject to sampling by PSDs, unless the solute’s affinity for the PSD-polymer is stronger than

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for particles suspended in the water. Such samplers have been used for example for poly aromatic

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hydrocarbons (PAHs) in stormwater drainage wells,10 heavy metals in the inlet and outlet from a

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stormwater detention pond,11 and as a semi-quantitative approach to source tracing of metals in sewer

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systems.12 The advantages of PSDs are lower costs for equipment and that the measurements are

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integrated over time-periods of weeks to months, increasing the period represented by each sample

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compared with e.g. grab sampling or flow proportional sampling. Most PSDs however collect solutes in

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a time-integrative manner. When deploying time-integrative PSDs over periods of e.g. one month in a

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highly dynamic storm drainage system with long periods without flow, the resulting sample will be

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dominated by the concentration in the adjacent stagnant water during dry weather and not by the

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concentrations occurring during runoff. The optimal PSD for stormwater runoff would therefore sample

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proportionally to the flow in the system.

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In recent years research has been conducted on a new passive sampling technique, which is based on

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advective flow of water through the PSD (called SorbiCell).13 Successful application of this sampler has

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been reported for measuring nitrate and phosphorous in surface waters and drainage water with a time-

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integrative installation method,14 and sorbents are available for sampling a range of heavy metals,

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volatile organic compounds, PAHs, pesticides and nutrients (www.sorbisense.com). The construction of

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this flow-through sampler allows installing it in a new way, which produces velocity dependent

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measurements that are appropriate when evaluating loads or flow weighted mean concentrations related

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to dynamic discharge of pollutants. This velocity dependent passive sampling method may thus

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potentially revolutionize monitoring of stormwater systems.

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The aim of the work presented here is to test the new velocity dependent installation method for the

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flow-through PSD in stormwater runoff. We focus on the heavy metals Cu, Zn and Pb at realistically

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low concentrations, but the results are in principle valid for any dissolved micropollutant or

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micropollutants sorbed to small particles for which appropriate sorbents are available. In order to

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evaluate the precision of the PSD measurements, replicate PSDs were deployed. In order to evaluate the

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accuracy of the PSD measurements, volume proportional samples were taken during parts of the

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deployment period of the PSDs. However, we recognize that the ‘true value’ cannot be found for such ACS Paragon Plus Environment

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complicated systems irrespective of the chosen sampling approach (there are always uncertainties and

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biases connected with sampling methods in stormwater).8,15 Furthermore, an uncertainty-calibrated16

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dynamic stormwater quality model,17 was used to evaluate loads and concentrations during the whole

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deployment period including periods where no volume proportional samples were taken, in order to

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validate the long-term average concentrations measured with velocity dependent passive sampling.

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THEORY

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Flow-through passive samplers

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The flow-through PSD used here (SorbiCell), consists of a cartridge (6.5 cm long and 1 cm in outer

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diameter) containing a macro-porous chelating resin sorbent (mesh particle size of 16-50) suitable for

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sampling of e.g. Hg, Pb, Cu, Cd and a tracer salt (calcium-citrate tetrahydrate) held in the cartridge by a

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spheriglass filter.13 When water passes through the cartridge, target analytes accumulate on the sorbent

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and tracer salt is washed out proportionally to the passing water volume. The water volume that has

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passed through the sampler during deployment (V) is then given by the equation: V=(Mt,0-Mt)/Ct,max

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where Mt,0 is the initial tracer mass, Mt is the final remaining tracer mass after installation, and Ct,max is

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the concentration of the tracer ion in solution.13 The concentration of analyte, Ca, is given by: Ca=Ma/V,

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where Ma is the mass of analyte exracted from the PSD.13 A spheriglass filter in front of the sorbent

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(100-160 µm) prevents larger particles from entering the sampler.

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Assumptions behind installation of passive samplers for velocity dependent sampling

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The principle behind the installation of PSDs for velocity dependent sampling is that the PSD is

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placed directly in the stormwater flow. During runoff events water passes through the cartridge because

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of the velocity head created by the flowing water. This method would, if the sampling was truly flow-

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proportional and if the event runoff volume was known, result in an average measurement, which

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represents the flow-weighted average concentration during runoff or the load of a pollutant passing the

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sampling point during the deployment period. The assumptions which are necessary in order to regard

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this sampler as flow-proportional are (a) that there is no uptake in the sampler when there is no flow in ACS Paragon Plus Environment

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the system, (b) that the water velocity is linearly proportional to water flow at the site, (c) that the water

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velocity at the sampling point is representative of the velocity over the whole flow cross-section, (d) that

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the water velocity at the site is proportional to water flow through the sampler and the relationship is not

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changing over time, and (e) that the total concentration is captured in the samplers (not only a fraction

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of the pollutant such as the dissolved fraction). Further theory to elucidate these assumptions is given

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below.

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(a) Uptake in the sampler during no flow

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The main uptake of analytes in the sampler is through advective flow through the sampler. Diffusion

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will however result in uptake when there is no flow in the system. This can potentially bias the sampling

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because analytes accumulate on the sorbent without wash-out of the tracer salt. It is well known that for

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PSDs based on diffusion, the sampling rate varies linearly with surface area of the sampler.18-20 In order

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to limit the diffusive uptake of analytes in the sampler during dry weather periods without flow,

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diffusion to the sorbent is therefore limited through a small opening of the sampler. The maximum

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sampling rate Rs,max during no flow can be estimated by assuming that the water boundary layer (WBL)

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is rate limiting for the diffusion of analytes to the sorbent:18 

,  ∙

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(1)

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where Rs is the sampling rate of the sampler (volume of water per time e.g. L/d), A is the cross-section

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area of the sampler, Dw is the aqueous diffusion coefficient of the pollutant, and δw is the thickness of

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the WBL

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(b) Velocity and flow relationship

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The relationship between velocity and flow depends on the geometry and conditions of the monitored

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system. If both flow and velocity is measured, the impact of weighting concentrations according to

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velocity rather than according to flow can be estimated using a dynamic stormwater runoff quality

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simulation model. This can be done by considering the measured flow and velocity and for each time-

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step during a runoff event and weight the concentrations simulated by the simulation model (for the

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same runoff event) in order to find an estimated velocity weighted event mean concentration (EMCv)

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and an estimated flow weighted event mean concentration (EMCq): 

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  ∑ ∑

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  ∑ ∑

 



 

∙ 

(2)

∙ 

(3)

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where vi and qi are the ith measurements of velocity and flow, respectively, Ci is the pollutant

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concentration in the ith measurement, and n is the number of velocity and flow measurements during the

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runoff event.

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(c) Cross-sectional velocity profile

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The velocity of the water at the sampling point depends on the relative depth of installation as well as

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the currents at the site. For relative depths of 0.1-1, the relative velocity in open channels is within

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approximately 0.9-1.1 for turbulent flows, which can safely be assumed in stormwater runoff.21

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(d) Relationship between runoff velocity and flow through the sampler

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The relationship between water velocity and flow through the samplers has been tested in a flow-

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channel by Kronvang et al.22 who found R2 = 0.77 for 1 week installations and R2 = 0.57 for 2 week

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installations at 0.05-0.3 m/s. Change in this relationship over time can be caused by either instant

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clogging if leaves or other ‘large’ objects get stuck on the sampler or slow clogging where small

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particles captured in the sampler change the conductivity of the sampler over time. If slow clogging

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occurs, it will lead to higher weighting of runoff during the first part of the sampling period than during

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the last part. Also changes in the hydraulics around the sampler may have influence on the relationship

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between runoff velocity and flow through the sampler. In both cases it is important to notice, that if a

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peak concentration occurs either when the sampler is partially clogged or when the hydraulics around

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the sampler disfavor sampling, this may have a negative effect on how much analyte is captured in the

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sampler. But if intermittent clogging occurs and the water has average concentrations, it will not have an

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influence on the evaluated concentrations.

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Another important issue is the fraction of the analytes which is sampled by the PSD. The freely

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dissolved and labile species are retained by the sorbent, which by design has a high affinity for the

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analytes (here the heavy metals Cu, Zn and Pb). However, particles (including pollutants sorbed to the

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particles) which are small enough to enter the sampler can also be captured in the sampler and therefore

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included in the analysis. According to the manufacturer it is often seen that coloring of the polymer

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material from e.g. humic material is more pronounced in the top of the cartridge, but after extreme flow

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events coloring in the bottom of the cartridge is also experienced, and when sampling phosphorus the

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PSD results correlate much better with traditional measurements of total phosphorous than with the

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dissolved species orthophosphate.23 Other studies have found that heavy metals in stormwater were

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either dissolved or mainly sorbed to particles smaller than 150 µm,24 that the main sources of traffic

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related heavy metals were associated with particle sizes