recycling waste waters in a petrochemical site

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This project has received funding from the European Union’s Seventh Programme for research, technological development and demonstration under grant agreement No 280756. RECYCLING WASTE WATERS IN A PETROCHEMICAL SITE Speakers : Christine BERTRAND (TOTAL), Audrey BRETON (TOTAL) Contributors : Alexandre MULLER (TOTAL), Carole BAILLY (TOTAL), Nicolas LESAGE (TOTAL), Sarah CHERET (SUEZ), Sylvie BAIG (SUEZ), Nienke KOEMAN (TNO), Raymond CREUSEN (TNO), Angeles BLANCO (UCM), Daphne HERMOSILLA (UCM), Helen BARNDOK (UCM) Team on site: Lydie MULON (TOTAL), Bruno RUFFIN (TOTAL), Laura DIGAN (TOTAL), François FAUQUET (TOTAL), Martine JOUANOLOU (TOTAL), Hervet NABET (TOTAL), Thierry FESTY (TOTAL), Eric LEROY (TOTAL) Alix BOURDASSOL (TOTAL) , Carole DUMONT (TOTAL)

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Page 1: RECYCLING WASTE WATERS IN A PETROCHEMICAL SITE

This project has received funding from the European Union’s Seventh Programme for research, technological development and demonstration under grant agreement No 280756.

RECYCLING WASTE WATERS IN A PETROCHEMICAL SITE

Speakers : Christine BERTRAND (TOTAL), Audrey BRETON (TOTAL) Contributors : Alexandre MULLER (TOTAL), Carole BAILLY (TOTAL), Nicolas LESAGE (TOTAL), Sarah CHERET (SUEZ), Sylvie BAIG (SUEZ), Nienke KOEMAN (TNO), Raymond CREUSEN (TNO), Angeles BLANCO (UCM), Daphne HERMOSILLA (UCM), Helen BARNDOK (UCM)

Team on site: Lydie MULON (TOTAL), Bruno RUFFIN (TOTAL), Laura DIGAN (TOTAL), François FAUQUET (TOTAL), Martine JOUANOLOU (TOTAL), Hervet NABET (TOTAL), Thierry FESTY (TOTAL), Eric LEROY (TOTAL) Alix BOURDASSOL (TOTAL) , Carole DUMONT (TOTAL)

Page 2: RECYCLING WASTE WATERS IN A PETROCHEMICAL SITE

E4Water, Final Conference, April 19-20 2

RECYCLING WASTE WATERS IN A PETROCHEMICAL SITE

Petrochemical site

TOTAL Gonfreville Plant Normandy, France Fresh Water annual use is

7 Million m3

Page 3: RECYCLING WASTE WATERS IN A PETROCHEMICAL SITE

This project has received funding from the European Union’s Seventh Programme for research, technological development and demonstration under grant agreement No 280756.

Reducing water intake by 40% Improve the quality of waste waters for compliance with current and future regulations Find alternative or complement to the classical use of biocides for cooling waters Improve the quality of cooling waters for compliance with future regulations

CW SF

UV

O3

CW

Nonylphenols Benzo(a)pyrene

Chloroform

E4WATER objectives TOTAL Case

WW O3 BIO UF RO

CW PW

Page 4: RECYCLING WASTE WATERS IN A PETROCHEMICAL SITE

This project has received funding from the European Union’s Seventh Programme for research, technological development and demonstration under grant agreement No 280756. Reducing water intake by 40%

Improve the quality of waste waters for compliance with current and future regulations Find alternative or complement to the classical use of biocides for cooling waters Improve the quality of cooling waters for compliance with future regulations

CW SF

UV

O3

CW

Nonylphenols Benzo(a)pyrene

Chloroform

E4WATER objectives TOTAL Case

WW O3 BIO UF RO

CW PW

Page 5: RECYCLING WASTE WATERS IN A PETROCHEMICAL SITE

E4Water, Final Conference, April 19-20 5

SAVING 40% OF FRESHWATER !

783 m3/h of freshwater are used for cooling and demineralized water

Saving 40% of the fresh water need means saving 315 m3/h

Page 6: RECYCLING WASTE WATERS IN A PETROCHEMICAL SITE

E4Water, Final Conference, April 19-20 6

OPERATED TREATMENT CHAIN

2013 2016

May 2013 Start of the project

E4WATER

Pilot operations

July 2013 Site audit

June 2014 O3 WW

Summer 2014 UF/RO

January 2014 Biofilter

Page 7: RECYCLING WASTE WATERS IN A PETROCHEMICAL SITE

E4Water, Final Conference, April 19-20 7

DEVELOP AN INNOVATIVE LOW LIQUID DISCHARGE SYSTEM

Waste waters : what technology for what purposes ?

Wastewater after pre-deoiling

Reuse Reuse

Ozonation Biofiltration Ultrafiltration Reverse Osmosis

1st stage: Chemical/Biological oxidation Bulk organic matter Micropollutants (PAHs, BTEX) Solids

2nd stage: Ultrafiltration Solids

3rd stage: Reverse osmosis Salt content

Page 8: RECYCLING WASTE WATERS IN A PETROCHEMICAL SITE

E4Water, Final Conference, April 19-20 8

ENHANCED DEGRADATION OF ORGANICS

Synergetic combination of ozonation and biofiltration for COD removal (TRL 6)

Biofiltration : 50% Combined ozonation +

biofiltration : 70% PAHs and BTEX: <LQ

Wastewaterafter pre-deoiling

Reuse Reuse

Ozonation Biofiltration UltrafiltrationReverse Osmosis

Page 9: RECYCLING WASTE WATERS IN A PETROCHEMICAL SITE

E4Water, Final Conference, April 19-20 9

LAST STEPS FOR REUSING WASTE WATERS: SALT CONTROL

Wastewaterafter pre-deoiling

Reuse Reuse

Ozonation Biofiltration UltrafiltrationReverse Osmosis

Ultra filtration is key and needs close follow-up (TRL 6) Recovery rate 87% Performances in line with reverse osmosis protection

Reverse osmosis performances are adapted to waste water recycling for process operations (TRL 6) Recovery rate 75% Mitigate the salt content

Page 10: RECYCLING WASTE WATERS IN A PETROCHEMICAL SITE

This project has received funding from the European Union’s Seventh Programme for research, technological development and demonstration under grant agreement No 280756. Reducing water intake by 40%

Improve the quality of waste waters for compliance with current and future regulations Find alternative or complement to the classical use of biocides for cooling waters Improve the quality of cooling waters for compliance with future regulations

CW SF

UV

O3

CW

Nonylphenols Benzo(a)pyrene

Chloroform

WW O3 BIO UF RO

reuse reuse E4WATER objectives

TOTAL Case

Page 11: RECYCLING WASTE WATERS IN A PETROCHEMICAL SITE

E4Water, Final Conference, April 19-20 11

IMPROVE THE WATER LOOP OF THE COOLING TOWER IN THE PETROCHEMICAL SITE

Test alternative (or complement) sustainable technologies to challenge chemicals used in cooling towers Reduce the use of chemicals Reduce the environmental impacts (AOX)

Page 12: RECYCLING WASTE WATERS IN A PETROCHEMICAL SITE

E4Water, Final Conference, April 19-20 12

2013 2016

May 2013 Start of the project

E4WATER

Pilot operations September 2013

Sand filter March 2014

UV light cooling

July 2013 Site audit

May 2014 O3 cooling

TREATMENT CHAIN OPERATED

Page 13: RECYCLING WASTE WATERS IN A PETROCHEMICAL SITE

E4Water, Final Conference, April 19-20 13

TSS CONTROL IN COOLING SYSTEMS AS A PRELIMINARY STEP IS KEY

Appropriate to preserve downstream disinfection (TRL6) Cross flow microsand filtration

Max TSS outlet at 5 mg/L in normal

operation

Low water loss: <0.5%

Cooling water

Sand filtration

Ozonation

UV

Page 14: RECYCLING WASTE WATERS IN A PETROCHEMICAL SITE

E4Water, Final Conference, April 19-20 14

UV or O3 may be alternatives or complements to routine biocide treatment (TRL 6)

UV OR O3 DISINFECTION OF COOLING WATERS : IT WORKS

Cooling water

Sand filtration

Ozonation

UV

Fully inactivate microorganisms and control biofilm growth (0.5 mgO3/L; 350 mJ/cm²)

Without noticeable change in corrosion behavior

Page 15: RECYCLING WASTE WATERS IN A PETROCHEMICAL SITE

This project has received funding from the European Union’s Seventh Programme for research, technological development and demonstration under grant agreement No 280756. Reducing water intake by 40%

Improve the quality of waste waters for compliance with current and future regulations Find alternative or complement to the classical use of biocides for cooling waters Improve the quality of cooling waters for compliance with future regulations

CW SF

UV

O3

CW

Nonylphenols Benzo(a)pyrene

Chloroform

WW O3 BIO UF RO

CW PW E4WATER Conclusion

TOTAL Case

Page 16: RECYCLING WASTE WATERS IN A PETROCHEMICAL SITE

E4Water, Final Conference, April 19-20 16

NEW WATER MANAGEMENT SYSTEM

Low liquid discharge scheme Small saline stream is issued

Page 17: RECYCLING WASTE WATERS IN A PETROCHEMICAL SITE

E4Water, Final Conference, April 19-20 17

NEW WATER MANAGEMENT SYSTEM

Reduction in fresh water withdrawal:

40%

Reduction of waste water discharge: 59%

Decrease in emissions by COD : 92t / yr TSS : 32t / yr AOX : 0.3t / yr

OPEX: 0.36 €/m3 of fresh water saved/yr CAPEX: depend on local conditions Increase in energy consumption

Alternative or complement to

routine biocides

Page 18: RECYCLING WASTE WATERS IN A PETROCHEMICAL SITE

This project has received funding from the European Union’s Seventh Programme for research, technological development and demonstration under grant agreement No 280756.

RECYCLING WASTE WATERS IN A PETROCHEMICAL SITE

Thank you for your attention