COMPARISON OF THE IMPACT OF 3 HANDLING PROCESSES ON THE - - PowerPoint PPT Presentation

comparison of the impact of 3 handling processes on the
SMART_READER_LITE
LIVE PREVIEW

COMPARISON OF THE IMPACT OF 3 HANDLING PROCESSES ON THE - - PowerPoint PPT Presentation

COMPARISON OF THE IMPACT OF 3 HANDLING PROCESSES ON THE CHARACTERISTICS OF WASTEWATER SLUDGE M. Collard, B. Teychen, L. Leme laurent.lemee@univ-poitiers.fr ic2mp.labo.univ-poitiers.fr Limassol, Cyprus, 23 June 2016 1 Wastewater treatment


slide-1
SLIDE 1

COMPARISON OF THE IMPACT OF 3 HANDLING PROCESSES ON THE CHARACTERISTICS OF WASTEWATER SLUDGE

  • M. Collard, B. Teychené, L. Lemée

laurent.lemee@univ-poitiers.fr ic2mp.labo.univ-poitiers.fr

1 Limassol, Cyprus, 23 June 2016

slide-2
SLIDE 2

But could also be considered as an unlimited resource for

  • Water via re-use,
  • Energy (methane),
  • Phosphorous,
  • Fertilizer

treatment generates sludge

Wastewater

(13 Mt dry sludge expected by 2020)

Limassol, Cyprus, 23 June 2016 2

slide-3
SLIDE 3

Landfarming

main solution for sludge management (72%),

  • sustainable contrarily to incineration or landfill
  • accelerates the restoration of soils
  • reverse global warming (4%0 initiative)

Limassol, Cyprus, 23 June 2016 3

slide-4
SLIDE 4

Implemented prior to land farming, aims at

  • Reducing the volume thus transportation cost
  • producing energy
  • Sanitizing (stabilizing)
  • Improving agronomic properties
  • Degrading contaminants

Handling process

Limassol, Cyprus, 23 June 2016 4

slide-5
SLIDE 5

Evaluate the impact of processes on sludge characteristics, to envisage the environmental fate of this organic matter

Objective

Compared dried, irradiated and digested sludge at the global and molecular scale

Limassol, Cyprus, 23 June 2016 5

slide-6
SLIDE 6

Wastewater treatment plant of Poitiers (France)

Limassol, Cyprus, 23 June 2016 6

slide-7
SLIDE 7

Floated sludge 3L sludge

  • 1 kGy (sanitisation dose)
  • 50 kGy
  • Dried sludge 85°C
  • Pellets 120°C

AOP : HO• and e-

aq

4 weeks Thermal drying treatment plant Digestion Laboratory-scale digester e-beam irradiation real scale pilot

Limassol, Cyprus, 23 June 2016 7

slide-8
SLIDE 8

Infrared Spectroscopy

 O-H , N-H  C=C  C=O  C-H δ C-O

0,05 0,07 0,09 0,11 0,13 0,15 0,17

1 kGy IC-O/C-H 50

Increase for e-beam  oxydation of OM

Limassol, Cyprus, 23 June 2016 8

slide-9
SLIDE 9

Chemical fractionation

« Humin » « humic Acids » « fulvic Acids» Lipids sludge residue CH2Cl2/MeOH HCl NaOH

acido-soluble alcalino-soluble

  • rgano-soluble

Limassol, Cyprus, 23 June 2016 9

slide-10
SLIDE 10

Changes in soluble fractions

20 40 60 80 100

Floated sludge dried 85°C pellets 120°C 1 kGy 50 kGy 1 w 2 w 3 w 4 w Lipids Fulvic acids Humic acids Humin ash

Weakening at 120°C Decrease in OM and particularly lipids Digestion e-beam thermal

Impact of treatments at the global level

Limassol, Cyprus, 23 June 2016 10

slide-11
SLIDE 11

DSC: 2 exotherms

  • 1 : desorption of volatiles (350°C)
  • 2 : oxidation of heavy weight compounds (500°C)

TGA : Weight loss associated with exo1/exo2 increases with weakening of OM

Temperature

1 2

Weight loss (%) temperature difference(C/mg)

Thermal analysis

FS 85 120 0,50 0,55 0,60 0,65 0,70 0,75 0,80 0,85 0,90

WLexo1/exo2

Thermal drying

Limassol, Cyprus, 23 June 2016 11

slide-12
SLIDE 12

Double-shot pyrolysis

  • 1. low temperature : desorption of volatile molecules
  • 2. Higher temperature : breaks covalent bonds of high Mw

compounds

analyser ionisation

Pyrolysis = use of thermal energy only to break chemical bonds

Information at the molecular scale

GC MS

Limassol, Cyprus, 23 June 2016 12

slide-13
SLIDE 13

First-shot 350° C

‐0,1 0,1 0,2 0,3 0,4 0,5 0,6 20 40 60 80 100 120 200 400 600 800 1000 Tem perature ( ° C)

DSC

Thermal drying 120°

Fatty acids Steroïds

Limassol, Cyprus, 23 June 2016 13

slide-14
SLIDE 14

Second-shot 600° C

Aromatic monomers from refractory biopolymers (liginin, proteins, chitin,…)

‐0,1 0,1 0,2 0,3 0,4 0,5 0,6 20 40 60 80 100 120 200 400 600 800 1000 Tem perature difference( ° C/ m g) Tem perature ( ° C)

Thermal drying 120°

DSC

Limassol, Cyprus, 23 June 2016 14

slide-15
SLIDE 15

Double-shot pyrolysis

mg/g OM

Digestion e-beam thermal

10 20 30 40 50 60

floated sludge dried 85°C pellets 120°C 1 kGy 50 kGy 1 w 2 w 3 w 4 w

FaMe Sterols aromatics

  • Visible changes at the molecular level for FaMe and sterols

Limassol, Cyprus, 23 June 2016 15

slide-16
SLIDE 16

First-shot 350°C : fatty acids

C16 C18

plant Ion extract (m/z 74)

C17

  • Decrease with thermal drying
  • Stable after 2w digestion

Branched (i+a)/linear

floated 85 120

, , , , ,

Bacterial origin

i a n C15 i a n

Limassol, Cyprus, 23 June 2016 16

slide-17
SLIDE 17

First-shot 350°C : steroids

Stanols Sterols

Rstanols/sterols

Ion extract(m/z 213,215)

85°C floated 120°C

, , , , , , , , ,

Increase with thermal drying coprostanol cholesterol

Limassol, Cyprus, 23 June 2016 17

slide-18
SLIDE 18

18

  • Elemental analysis, Infrared spectroscopy :

decrease in OM content with 1kGy and digestion

  • xidation with e-beam
  • Chemical fractionation, thermal analysis :

Weakening with thermal drying and 50 kGy Complexification with 1 kGy

  • Py-GC/MS : information at the molecular scale

Changes in fatty acids and steroids Degradation of aromatics with e-beam only

Conclusion

Limassol, Cyprus, 23 June 2016

slide-19
SLIDE 19

Thanks for your attention

Limassol, Cyprus, 23 June 2016 19