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QSPR prediction of pharmaceutical removal with GAC

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Title: QSPR prediction of pharmaceutical removal with GAC


1
QSPR prediction of pharmaceutical removal with GAC
David de Ridder
Carbamazepine
Delft
2
Problem statementmicropollutants
  • 100.000 different micropollutants in surface
    water
  • Variable mixture
  • RIWA Rijn measures about 250 org. micropollutants
  • Analysis programs costly and time consuming
  • QSAR can be used as a screening tool

3
QSAR werkDavid de Ridder
  • Singular processes
  • Activated carbon (AC)
  • Aeration
  • Ozone
  • UV
  • Combinations of processes
  • AC-UV/H2O2-AC
  • (RBF)-NF-AC

4
Activated carbon Research objectives
  • Estimate
  • Influence of turbulence on adsorption kinetics
  • Influence of water quality
  • Influence of preloading carbon
  • Construction of QSPR model
  • Accuracy of QSPR prediction Ce, qe

5
Experiment set-uppharmaceutical selection
- 0
6
Experiment set-upmatrix
7
Experiment set-up
  • 2 litre solution
  • Kinetic _at_ 200 mg carbon
  • Adsorption time 1 day 6
  • weeks
  • Equilibrium _at_ 20-2000 mg
  • carbon
  • Adsorption time 8 weeks
  • Carbon 0,63-0,71 mm

8
ResultsKinetic experiments
9
ResultsKinetic experiments
10
ResultsKinetic experiments
11
ResultsKinetic experiments
  • Lower turbulence decreases adsorption
    significantly
  • Preloading large influence on negatives, and no
    significant effect on positives.

12
Results - Equilibrium
13
Results - Equilibrium
14
Results - Equilibrium
15
Resultsinitial remarks
  • MW in range 200-300 D no significant influence
  • Log D has higher impact on removal of negatives
  • At similar pKa, higher log D yields higher
    removal
  • At similar log D, positives are removed 1,2-2
    times more effective than negatives
  • In wastewater
  • Positives comparable removal as surface water
  • Neutrals better removal than in surface water
  • Significant removal of 4 negatives in blank!

16
Resultshypotheses
  • Preloading creates a negatively charged layer
    onto the carbon, rejecting negatives and
    attracting positives
  • In the MW range of 200-300 D, probably most
    carbon micropores will be available for
    adsorption
  • In wastewater, (bio)degradation of negatives is
    preferred.

17
Results - QSPR construction
  • 4 (out of 21) compounds excluded for verification
  • MLR (multivariable linear regression) prediction
    model

18
Results - QSPR prediction
19
Results - QSPR validation
20
Results model accuracy
Consequent over/underprediction Less data
available
Specific mispredictions
21
Results Freundlich parameters
22
Initial conclusionsModel prediction
  • Applied carbon dose too high -gt ultrapure models
    inaccurate
  • Initial degradation negatives wastewater -gt
    negatives not taken properly into account
  • Surface water general underprediction Ce at
    higher carbon dose
  • Wastewater Specific overprediction Ce
    (Terbutaline, Salbutamol, metropolol,
    Clenbuterol, Aminopyrine)
  • Demiwater PL consequent over/underprediction

23
Further research
  • Dataset
  • Larger variation MW (if relevant)
  • Process conditions
  • Carbon type
  • Change preparation preloaded carbon
  • Lower carbon doses
  • pH variation at same water quality (decrease
    charge negatives, lower log D negatives higher
    log D positives)
  • Analysis
  • ATP to check for biological activity
  • NOM characterisation (blank adsorbed (?))
  • Carbon characterisation (PSD, hydrophobicity,
    carbon pKa)

24
Questions/remarks?
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