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Presentation - National Water Research Institute

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Characterisation of Organic Matter in Alum Treated<br />

Drinking <strong>Water</strong> using Reverse Phase‐High<br />

Performance Liquid Chromatography and<br />

Ion‐Exchange Resins<br />

Dongsheng Wang 1,2 , Linan Xing 1 , Mohamad Fared Murshed 2 , Theodore W.C. Lo 3 ,<br />

Rolando Fabris 4 , Christopher W.K. Chow 1,2,4 , John van Leeuwen 1,2 , Mary Drikas 1,2,4<br />

1 State Key Lab of Environmental Aquatic Chemistry, RCEES, CAS, Beijing, China.<br />

2 SA <strong>Water</strong> Centre for <strong>Water</strong> Management and Reuse, University of South Australia, Mawson Lakes,<br />

South Australia, Australia.<br />

3. Laboratory Lb Animal lS Service Centre, The Chinese University i of Hong Kong, Prince Pi of Wl Wales Hospital,<br />

Shatin, Hong Kong.<br />

4<br />

Australian <strong>Water</strong> Quality Centre, SA <strong>Water</strong>, Adelaide, South Australia, Australia.


Outlines<br />

o Resin fractionation‐hydrophobicity & hydrophilicity<br />

o Characterization of NOM using RP‐HPLC<br />

o Key component of our RP‐HPLC approach<br />

o Comparison of resin fractionation method and<br />

RPHPLC for NOM<br />

o Impact of coagulation on chromatographic behaviour


Resin fractionation<br />

~ Resin fractionation has been introduced to<br />

determine hydrophobicity of NOM in order to<br />

optimize coagulation performance<br />

~ Resin fractionation is based on adsorption onto<br />

different absorbent resins by calculated the organic<br />

concentration before and after contact with resins.<br />

• An early case study in Australia has demonstrated dthe link<br />

between source water hydrophobic fraction and<br />

coagulant dose<br />

• By characterising organics based on their hydrophobicity<br />

and hydrophilicity, the treatability of NOM can be<br />

determined


Earlier work on resin fractionation<br />

Chow, C.W.K., Fabris R. and Drikas, M. (2004) A Rapid<br />

Fractionation Technique To Characterise Natural Organic<br />

Matter For The Optimisation Of <strong>Water</strong> Treatment Processes. J<br />

<strong>Water</strong> SRT – Aqua 53(2) 85‐92.<br />

Chow, C.W.K., Fabris R., Drikas, M. and Holmes, M. (2005) A<br />

Case Study of Treatment Performance and Organic Character.<br />

J<strong>Water</strong>SRT– Aqua 54(6) 385‐395.<br />

However, resin fractionation was recognized as a time<br />

consuming technique and new alternative technique<br />

using HPLC has been introduced


Characterization of NOM using RP HPLC<br />

→ Since 80’s, researchers use RP HPLC to characterize HA and FA.<br />

→ In recent years, people are working for finding standard materials to compare<br />

with the polarity of NOM. Moreover, they combine with other advanced<br />

techniques, such as:<br />

i. pyrolysis‐gas chromatography‐mass spectrometry (Py‐GC‐MS)<br />

ii. solid state 13 C‐NMR spectroscopy<br />

iii. diffuse reflectance infrared Fourier transform (DRIFT).<br />

→ However, most of them considered to consume considerable time and effort,<br />

and require relatively expensive and complex instrumentation.<br />

→ Therefore, this RP HPLC has been introduced which is:<br />

o The detections all based on concentration NOM samples<br />

o Recovery tends out between 70% to 200‐300%<br />

o there are size exclusion effect during the detection


Mechanism of RPHPLC<br />

‣ The principle of operation is that organic material in an<br />

aqueous solution is introduced to a hydrophobic bonded HPLC<br />

column (eg. C18) which adsorbs the hydrophobic materials<br />

while the hydrophilic materials remain in the carrier and exit<br />

immediately to the detector.<br />

‣ After a set time period, the phase of the eluent is changed to a<br />

predominantly polar organic solvent (ie. reversing the phase) and<br />

the adsorbed hydrophobic material is desorbed from the column<br />

and flows to the detector.


Key component of our RP HPLC approach<br />

a. Optimized Reverse Phase HPLC Liquid System Program<br />

b. Deterioration and reproducibility<br />

c. Background Correction<br />

b)<br />

0.08<br />

3 Repeat tInjections<br />

UV absorbance @ 254nm (cm -1 )<br />

0.07<br />

0.06<br />

0.05<br />

0.04<br />

0.03<br />

0.02<br />

0.01<br />

pure water<br />

Morgan raw<br />

Middle River raw<br />

MR<br />

MG<br />

MilliQ<br />

0.00<br />

0 5 10 15 20<br />

Retention time (min)


Key component of our RP HPLC approach<br />

d. Quantifying chromatography results using peak fitting<br />

• Peak fitting software (Version 4, Systat Software Inc.) was used to resolve peak<br />

components based on statistically ideal fits using various peak shapes<br />

• Total peak area removal for the RPHPLC profile was calculated by using the<br />

difference between the peak area of the resolved peaks (after peak fitting) of<br />

raw and treated water from the RPHPLC scans<br />

Peak 1 to 4 with low retention time were defined as the<br />

RPHPLC‐hydrophilic proportion<br />

Peak 5 to 7, detected at longer retention time, were<br />

defined as the RPHPLC‐hydrophobic proportion


Natural water sample selection‐High SUVA water<br />

Morgan – River Murray (<strong>Water</strong><br />

Source for South Australia)<br />

Middle River Reservoir –<br />

Kangaroo Island off the coast<br />

of South Australia<br />

Colour: 58 HU<br />

DOC: 8.8 88mg/L<br />

UV 254 : 0.325 cm ‐1<br />

SUVA: 3.7 m ‐1 mg ‐1 L<br />

Colour: 145 HU<br />

DOC: 12.4 mg/L<br />

UV ‐1<br />

254 : 0.660 cm<br />

SUVA: 5.0 m ‐1 mg ‐1 L


Comparison of resin fractionation method and<br />

RPHPLC for NOM<br />

RPHPLC profile of isolated resin sample…..<br />

Resin fractionation<br />

Percentage of peak area result using Peak fitting software<br />

the resin‐hydrophobic fraction<br />

not only contains RPHPLChydrophobic<br />

components but<br />

also RPHPLC‐hydrophilic<br />

components


Impact of coagulation on chromatographic behaviour<br />

A treatment simulation test, the ‘Jar test’ was conducted<br />

on Morgan and Middle river raw water<br />

Jar testing was performed at pH 5.5, 6, 7 and 8.5 at dose<br />

from low to high (60 – 200 mg/L)<br />

According to the profiles, it<br />

can be seen that with the<br />

increase in alum dose, both<br />

the hydrophobic and<br />

hydrophilic proportions<br />

decreased gradually


Impact of coagulation on chromatographic behaviour<br />

Peak 1 easily can be removed by<br />

coagulation<br />

Hydrophilic peak (2‐4) can be<br />

removed better than<br />

hydrophobic peak (5‐7)


Comparison of organic character of the recalcitrant organic at<br />

maximum DOC removal coagulation<br />

maximum DOC removal coagulation<br />

Molecular weight<br />

distribution<br />

‐ Max alum coagulation dose at 200 mg/L<br />

‐ the removal efficiency of the hydrophilic proportion (Peak 2‐4) is lower than that of<br />

the hydrophobic proportion (Peak 5‐7)<br />

‐ RPHPLC‐hydrophilic contains components of the resin‐hydrophobic fraction which is<br />

expected to be removed by coagulation.


Comparison with resin fractionation –Treated waters<br />

UV abs sorbance @ 254 nm<br />

(cm -1 )<br />

0.018<br />

0.015<br />

Middle River treated<br />

Hydrophpbic of Middle River treated<br />

Hydrophilic of Middle River treated<br />

The peak areas 0.012 of each peak for the treated Middle River water were higher than that of<br />

0.009<br />

treated Morgan 0.009 water.<br />

0.015<br />

0.012<br />

Morgan treated<br />

Hydrophobic of Morgan treated<br />

Hydrophilic of Morgan treated<br />

0.006<br />

However, the peak area percentages of resin hydrophobic and resin hydrophilic for the two<br />

0.003<br />

0.003<br />

treated t waters were similar<br />

il<br />

0.000<br />

10 100 1000 10000 100000<br />

Apparent molecular weight (Da)<br />

0.006<br />

0.000<br />

10 100 1000 10000 100000<br />

Apparent molecular weight (Da)


Comparison with resin fractionation –Treated waters<br />

Precentage Pea ak Area (%)<br />

100<br />

90<br />

80<br />

70<br />

60<br />

50<br />

40<br />

30<br />

20<br />

10<br />

0<br />

18 15 17 19<br />

16<br />

28<br />

24<br />

26<br />

33 28 37<br />

7<br />

26<br />

5<br />

10<br />

17<br />

21 12<br />

16 22 20<br />

14<br />

11 10<br />

9<br />

10 10<br />

8<br />

5<br />

5<br />

25 26<br />

12 13 11 13<br />

MG treated MR treated MG treated MR treated MG treated MR treated<br />

resin resin resin resin<br />

hydrophobic hydrophobic hydrophilic hydrophilic<br />

Peak 7<br />

Peak 6<br />

Peak 5<br />

Peak 4<br />

Peak 3<br />

Peak 2<br />

Peak 1<br />

‣ the DOC of the resin<br />

hydrophobic proportion<br />

isolated decreased from 7.2 72<br />

mg L ‐1 to 3.6 mg L ‐1 for<br />

Morgan water, while Middle<br />

River water decreased from<br />

11.2 mg L ‐1 to 5.6 mg L ‐1 .<br />

Their DOC removal<br />

efficiencies were both 50%.<br />

‣ The DOC resin hydrophilic value decreased from 1.6 mg L ‐1 to 0.8 mg L ‐1 for Morgan<br />

water, while Middle River water decreased from 1.3 mg L ‐1 to 1.1 mg L ‐<br />

‣ RPHPLC profiles of resin hydrophilic proportions of were compared and showed that,<br />

for the same water, the profiles before and after coagulation were very similar. This<br />

confirmed that resin hydrophilic compounds were recalcitrant to alum coagulation<br />

removal


Further statistical analysis using<br />

multiple regression analysis<br />

• % UV 254 removal = 0.012012 × % removal of Peak 1<br />

+ 0.97 × % removal of Peak 2‐4<br />

+ 0.026 × % removal of Peak 5‐7<br />

• % DOC removal = 0.0072 × % removal of Peak 1<br />

+ 0.79 × % removal of Peak 2‐4<br />

+ 021× 0.21 × % removal of Peak 5‐7<br />

• The R 2 values of both equations were 0.99.<br />

• This confirmed that it is possible to establish a relationship between<br />

RPHPLC peaks (resolved by the proposed peak fitting model) with<br />

treatability.


Conclusion<br />

The RPHPLC method developed and reported in this s paper was found to be reliable and<br />

convenient for characterizing detecting NOM raw and coagulated waters. It is important to<br />

be able to identify and evaluate the removable components of NOM during water<br />

treatment.<br />

This study confirmed that the hydrophilic portion was recalcitrant to conventional<br />

treatment . By combining with HPSEC method, this study also confirmed that the hydrophilic<br />

proportion was considered as low molecular weight compounds.<br />

It was found that the hydrophilic proportions isolated by the XAD procedure are all of small<br />

molecular weight and were recalcitrant to alum coagulation.<br />

The RPHPLC method should be a useful tool for the optimization of water treatment<br />

procedure by allowing assessment of the efficiencies of combinations of pre‐ozonation,<br />

enhanced coagulation and advanced oxidation processes.


Acknowledgement<br />

NSF of China under 51025830 and 50921064, <strong>National</strong> Basic<br />

<strong>Research</strong> Program of China under 2011CB9337005108<br />

South Australian Premier’s Science and <strong>Research</strong> Fund Project<br />

“Development of materials engineering solutions for treatment of<br />

Murray‐Darling Basin sourced water supplies”<br />

Special fund from the State Key Laboratory of Environmental<br />

Aquatic Chemistry, Project 08K08ESPCR<br />

SA <strong>Water</strong> and Australian <strong>Water</strong> Quality Centre, University of South<br />

Australia, Australia


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