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Development of SLL equilibrium speciation and data fitting tool and its application to P recovery process from sludge

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(1)

Development of SLL equilibrium

speciation and data fitting tool and

its application to P recovery process

from sludge

Z.A. Shariff, L. Fraikin, A. Léonard, A. Pfennig

za.shariff@uliege.be

Products, Environment, and Processes (PEPs)

Department of Chemical Engineering

University of Liège

https://www.chemeng.uliege.be

Jahrestreffen der ProcessNet-Fachgruppen

(2)

agenda

Introduction to P recycling

PULSE process

SLLE tool

results

summary

(3)

introduction

• essential element for all forms of life

• finite resource

• EU imports more than 90% of P

• sewage has potential to cover more

than 20% of P demand in

North-West Europe

(4)

PULSE (Phosphorus University of Liege

Sludge Extraction) process

acid

organic

solvent

base/Ca

drying

leaching

filtration

reactive

extraction

re-extraction

CaP

solid

waste

metals

precipitation

dewatered

sludge

waste

water

re-extraction

agent/NH

3

P + impurities

~20% DM

≥95% DM

(5)

PULSE process

leaching of P and metals from sludge

𝐹𝑒𝑃𝑂

4

+ 3𝐻𝐶𝑙 → 𝐹𝑒

3+

+ 𝐻

3

𝑃𝑂

4

+ 3𝐶𝑙

Reactive extraction of metals with organic solvent

Fe

3+

+ 4Cl

↔ FeCl

4

𝑅

3

𝑁𝐻𝐶𝑙 + 𝐹𝑒𝐶𝑙

4

↔ 𝐹𝑒𝐶𝑙

4

𝑅

3

𝑁𝐻 + 𝐶𝑙

Precipitation of CaP

(6)

why SLL equilibrium modelling

process development

evaluation of unit operations

deeper understanding

process optimization

(7)

charge balance (CB)

0 = σ

𝑖=0

𝑛

𝑐

𝑖

𝑧

𝑖

mass balance (MB)

𝐶𝑡𝑜𝑡

𝑗

= σ

𝑖=0

𝑛

𝜈

𝑖,𝑗

𝑐

𝑖

law of mass action (LMA)

𝑙𝑜𝑔𝐾

𝑚

= σ

𝑖=0

𝑛

𝜈

𝑖,𝑟

𝑙𝑜𝑔 𝑎

𝑖

FeCl

3

liquid phase speciation

FeCl

3

Fe

3+

Cl

-FeCl

2+

FeCl

2+

FeCl

4

-FeOH

2+

FeOH

2 +

FeOH

3

OH

-H

+

FeOH

4

-FeOH

3(s)

𝑎

𝑖

=

γ

𝑖

𝑐

𝑖

a

i

= activity of ith species

γ

𝑖

= activity coefficient

𝑐

𝑖

= concentration

(8)

𝐴𝐵

𝑠𝑜𝑙𝑖𝑑

↔ 𝜈

1

𝐴 + 𝜈

2

𝐵

from law of mass action

𝐾

𝑠𝑝

= 𝑎

𝐴0

𝜈

1

𝑎

𝐵0

𝜈

2

(at equilibrium)

Ion Activity product: 𝐼𝐴𝑃 = 𝑎

𝐴

𝜈

1

𝑎

𝐵

𝜈

2

(actual)

Saturation Index: 𝑆𝐼 = log 𝐼𝐴𝑃 – 𝑙𝑜𝑔 𝐾

𝑠𝑝

SI = 0:

IAP =

𝐾

𝑠𝑝

equilibrium

SI < 0:

IAP <

𝐾

𝑠𝑝

undersaturated (dissolution)

SI > 0:

IAP >

𝐾

𝑠𝑝

supersaturated (precipitation)

(9)

SLE MATLAB tool results

-1 0 1 2 3 4 5 6 7 8 9 1E-6 1E-5 1E-4 0.001 0.01 0.1 1

CaHPO

4

FeCl

4-FeHPO

Fe

2+

PO

4

3-CaHPO

4

(S)

AlPO

4

(S)

FePO

4

(S)

CaH

2

PO

4+

FeH

2

PO

42+

H

3

PO

4

H

2

PO

4-HPO

4

2-FeH

2

PO

4+

Ca

2+

Cl

-Al

3+

Fe

3+

con

cen

tra

tion

mo

l/l

pH

(10)

experimental v/s SLE speciation results

-1 0 1 2 3 4 5 6 0.0 0.1 0.2 0.3 0.4 0.5 0.6 0.7 de gr ee of P lea ching equilibrium pH HCl H2SO4 HNO3 HCl+HNO3 HCl+H2SO4 HNO3+H2SO4 H3PO4 model

(11)

non-linear data fitting

deviation of modelling results

complex nature of sludge

P and metals bound to organic matter

lack of thermodynamic data

fitting of multiple parameters - equilibrium

constants and reaction stoichiometry

(12)

metal extraction from sludge liquor

TBP 10%; Exxal 3%; diluent – Ketrul;

0 2 4 6 8 10 0.0 0.2 0.4 0.6 0.8 1.0 Pb Zn P Hg Fe Cu Cd As de gr ee of ext ra ction

(13)

0.01 0.1 1 0.0 0.2 0.4 0.6 0.8 1.0 E (experimental) E (model)

de

gr

ee

of

ext

ra

ction

(E)

Alamine 336 conc. mol/L

LLE - non-linear data fitting

𝐹𝑒𝐶𝑙

𝑚

+

𝑛𝑅

3

𝑁𝐻

+

𝐶𝑙

=

𝐹𝑒𝐶𝑙

𝑚

(𝑅

3

𝑁𝐻)

𝑛

+

𝑛𝐶𝑙

𝐿𝑜𝑔 𝐾 = 3.616

(14)

summary

MATLAB tool for simulation of SLLE with precipitation of

multiple solid phases

data fitting – lack of thermodynamic data and nature of

sludge

further development of the model

incorporate activity models for IS>1 mol/L

incorporate temperature dependence for logK

(15)

acknowledgements

we are thankful to

BTC Europe GmbH – BASF for providing

samples of Alamine336

TOTAL Belgium for providing samples of Ketrul

UGhent and Prayon for ICP analyses

(16)

Development of SLL equilibrium

speciation and data fitting tool and

its application to P recovery process

from sludge

Z.A. Shariff, L. Fraikin, A. Léonard, A. Pfennig

za.shariff@uliege.be

Products, Environment, and Processes (PEPs)

Department of Chemical Engineering

University of Liège

https://www.chemeng.uliege.be

Jahrestreffen der ProcessNet-Fachgruppen

(17)

References

 http://www.nweurope.eu/projects/project-search/phos4you-phosphorus-recovery-from-waste-water-for-your-life/

 Doetsch, P., Pinnekamp, Johannes, Montag, D., Rath, W., Grömping, M., 2010.

Rückgewinnung von Pflanzennährstoffen, insbesondere Phosphor aus der Asche von Klärschlamm (Abschlussbericht PASCH). Institut für Siedlungswasserwirtschaft der RWTH Aachen, Aachen.

 Morel, F., & Hering, J. G., 1993. Principles and applications of aquatic chemistry. New York (N.Y.): Wiley

 Carrayrou , J., Mosé , R., & Behra, P., 2002. New efficient algorithm for solving thermodynamic chemistry. AIChE, 894-904.

 Andalibi, M.R., Kumar, A.S., Srinivasan, B., Bowen, P.L., Scrivener, K.L., Ludwig, C.H., & Testino, A., 2018. On the mesoscale mechanism of synthetic calcium– silicate–hydrate precipitation: a population balance modeling approach. J. Mater. Chem. A, 6, 363

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