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D1.2Operational demo cases
CS1 - Tarragona
EURECAT & AITASA
2
The project leading to this application has received funding from the European Union’s
Horizon 2020 research and innovation programme under grant agreement No 869318
CS1: Tarragona
Lead partner:
Other partners:
3
The project leading to this application has received funding from the European Union’s
Horizon 2020 research and innovation programme under grant agreement No 869318
CS1: Situation before Ultimate
 The Tarragona and Vilaseca-Salou wastewater treatment plants (WWTPs) were interconnected by a 4-km pipeline to ensure
that the AWRP can be supplied with enough secondary effluent from either or both WWTPs. Secondary effluent undergoes a
basic water reclamation process at the WRP (1021 m3/h average inlet flow rate), consisting of a ballasted clarification step
(Actiflo® unit), followed by disc filtration (DiscFilter® unit), multimedia filtration and sand filtration. The effluent undergoes an
advanced reclamation process including a two-pass reverse osmosis (RO) treatment processes and disinfection, using ultra-
violet light and chlorine, before it enters the reclaimed water distribution system.
Furthermore, chemical reagents such as coagulant, flocculent and antiscaling are added to enhance the plant performance.
 On the other hand, in order to meet future water requirements (BREF limits), an industrial wastewater treatment plant
(iWWTP) has been commissioned in April 2022 to polish the aggregated wastewater from the petrochemical complex and to
produce reclaimed water for the complex (1348 m3/h average water flow rate). The technology train to be implemented in
these new facilities will be:
- Dissolved air flotation (DAF)
- Biological membranes (MBR)
- Granular activated carbon (GAC)
4
The project leading to this application has received funding from the European Union’s
Horizon 2020 research and innovation programme under grant agreement No 869318
CS1: Objectives of the Ultimate solutions
5
The project leading to this application has received funding from the European Union’s
Horizon 2020 research and innovation programme under grant agreement No 869318
CS1: Objectives of the Ultimate solutions
OBJECTIVE:
Increase reclaimed water availability for the
complex by 20%:
 Current WWRP:
 Increase water recovery of the current WWRP
with nZLD technologies
 Remove the ammonium with low-cost
technology (zeolite adsorption)
 Future iWWTP:
 Defining a novel tertiary treatment with nZLD
technologies (reverse osmosis and membrane
distillation) to obtain reclaimed water
6
The project leading to this application has received funding from the European Union’s
Horizon 2020 research and innovation programme under grant agreement No 869318
CS1: Status/progress
Subtask: 1.2.1 Increasing reclaimed water availability of the petrochemical complex of Tarragona (ES)
Baseline technology: WWRP (pre-treatment+MF+SF+2-pass RO), iWWTP in operation in April 2022.
TRL: 57 (membranes), 56 (adsorption on zeolites)
Ultimate solution to foster circular economy:
Capacity: 12 m³/day
Quantifiable target: <20% reduction of fresh water through reuse of treated wastewater; 10 % reduction of energy demand
ULTIMATE: removal of ammonia
Status/progress:
• Bench scale experiments finished (UF, RO, MD and adsorption on zeolites)
• Pilot plant ordered (two different suppliers)
• Adsorption process designed by Eurecat/AITASA
7
The project leading to this application has received funding from the European Union’s
Horizon 2020 research and innovation programme under grant agreement No 869318
CS1: Pictures/videos of the new technologies
Subtask: 1.2.1 Increasing reclaimed water availability of the petrochemical complex of Tarragona (ES)
8
The project leading to this application has received funding from the European Union’s
Horizon 2020 research and innovation programme under grant agreement No 869318
CS1: Operational procedures and methodologies
Subtask: 1.2.1 Increasing reclaimed water availability of the petrochemical complex of Tarragona (ES)
• Work at bench scale is finished.
• Pilot plant:
• UF+ batch RO pilot plant ordered to supplier 1
• MD pilot plant ordered to supplier 2
• Adsorption pilot plant designed by Eurecat/AITASA
• AITASA is preparing the pilot plant location (pilot plant will be inside a 40 ft maritim container)
9
The project leading to this application has received funding from the European Union’s
Horizon 2020 research and innovation programme under grant agreement No 869318
CS1: Task 1.2.1 – Timeline
Subtask: 1.2.1 Increasing reclaimed water availability of the petrochemical complex of Tarragona (ES)
T1.2.1 - Increasing reclaimed water availability of the petrochemical
complex of Tarragona
Baseline conditions assessed MS05 D1.1
Design of pilot system MS09
Bench scale experiments MS15
Pilot system operational MS15 +7M D1.2 + 1M
Start-up & results MS19 D1.9
Best practices for water recycling D1.3
M1
M2
M3
M4
M5
M6
M7
M8
M9
M10
M11
M12
M1
M2
M3
M4
M5
M6
M7
M8
M9
M10
M11
M12
M1
M2
M3
M4
M5
M6
M7
M8
M9
M10
M11
M12
M1
M2
M3
M4
M5
M6
M7
M8
M9
M10
M11
M12
YEAR 1 YEAR 2 YEAR 3 YEAR 4
 Pilot system will be operational in June 2022 (M25)
 Still enough time to complete the pilot experiments
Legend
Task/Subtask
Activity as planned
Postponed activity
Delay of activity
The project leading to this application has received funding from the European Union’s
Horizon 2020 research and innovation programme under grant agreement No 869318
CS1 Contacts
sandra.casas@eurecat.org
andrea.naves@eurecat.org

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D1.2-Demonstrator Case Study Tarragona

  • 1. D1.2Operational demo cases CS1 - Tarragona EURECAT & AITASA
  • 2. 2 The project leading to this application has received funding from the European Union’s Horizon 2020 research and innovation programme under grant agreement No 869318 CS1: Tarragona Lead partner: Other partners:
  • 3. 3 The project leading to this application has received funding from the European Union’s Horizon 2020 research and innovation programme under grant agreement No 869318 CS1: Situation before Ultimate  The Tarragona and Vilaseca-Salou wastewater treatment plants (WWTPs) were interconnected by a 4-km pipeline to ensure that the AWRP can be supplied with enough secondary effluent from either or both WWTPs. Secondary effluent undergoes a basic water reclamation process at the WRP (1021 m3/h average inlet flow rate), consisting of a ballasted clarification step (Actiflo® unit), followed by disc filtration (DiscFilter® unit), multimedia filtration and sand filtration. The effluent undergoes an advanced reclamation process including a two-pass reverse osmosis (RO) treatment processes and disinfection, using ultra- violet light and chlorine, before it enters the reclaimed water distribution system. Furthermore, chemical reagents such as coagulant, flocculent and antiscaling are added to enhance the plant performance.  On the other hand, in order to meet future water requirements (BREF limits), an industrial wastewater treatment plant (iWWTP) has been commissioned in April 2022 to polish the aggregated wastewater from the petrochemical complex and to produce reclaimed water for the complex (1348 m3/h average water flow rate). The technology train to be implemented in these new facilities will be: - Dissolved air flotation (DAF) - Biological membranes (MBR) - Granular activated carbon (GAC)
  • 4. 4 The project leading to this application has received funding from the European Union’s Horizon 2020 research and innovation programme under grant agreement No 869318 CS1: Objectives of the Ultimate solutions
  • 5. 5 The project leading to this application has received funding from the European Union’s Horizon 2020 research and innovation programme under grant agreement No 869318 CS1: Objectives of the Ultimate solutions OBJECTIVE: Increase reclaimed water availability for the complex by 20%:  Current WWRP:  Increase water recovery of the current WWRP with nZLD technologies  Remove the ammonium with low-cost technology (zeolite adsorption)  Future iWWTP:  Defining a novel tertiary treatment with nZLD technologies (reverse osmosis and membrane distillation) to obtain reclaimed water
  • 6. 6 The project leading to this application has received funding from the European Union’s Horizon 2020 research and innovation programme under grant agreement No 869318 CS1: Status/progress Subtask: 1.2.1 Increasing reclaimed water availability of the petrochemical complex of Tarragona (ES) Baseline technology: WWRP (pre-treatment+MF+SF+2-pass RO), iWWTP in operation in April 2022. TRL: 57 (membranes), 56 (adsorption on zeolites) Ultimate solution to foster circular economy: Capacity: 12 m³/day Quantifiable target: <20% reduction of fresh water through reuse of treated wastewater; 10 % reduction of energy demand ULTIMATE: removal of ammonia Status/progress: • Bench scale experiments finished (UF, RO, MD and adsorption on zeolites) • Pilot plant ordered (two different suppliers) • Adsorption process designed by Eurecat/AITASA
  • 7. 7 The project leading to this application has received funding from the European Union’s Horizon 2020 research and innovation programme under grant agreement No 869318 CS1: Pictures/videos of the new technologies Subtask: 1.2.1 Increasing reclaimed water availability of the petrochemical complex of Tarragona (ES)
  • 8. 8 The project leading to this application has received funding from the European Union’s Horizon 2020 research and innovation programme under grant agreement No 869318 CS1: Operational procedures and methodologies Subtask: 1.2.1 Increasing reclaimed water availability of the petrochemical complex of Tarragona (ES) • Work at bench scale is finished. • Pilot plant: • UF+ batch RO pilot plant ordered to supplier 1 • MD pilot plant ordered to supplier 2 • Adsorption pilot plant designed by Eurecat/AITASA • AITASA is preparing the pilot plant location (pilot plant will be inside a 40 ft maritim container)
  • 9. 9 The project leading to this application has received funding from the European Union’s Horizon 2020 research and innovation programme under grant agreement No 869318 CS1: Task 1.2.1 – Timeline Subtask: 1.2.1 Increasing reclaimed water availability of the petrochemical complex of Tarragona (ES) T1.2.1 - Increasing reclaimed water availability of the petrochemical complex of Tarragona Baseline conditions assessed MS05 D1.1 Design of pilot system MS09 Bench scale experiments MS15 Pilot system operational MS15 +7M D1.2 + 1M Start-up & results MS19 D1.9 Best practices for water recycling D1.3 M1 M2 M3 M4 M5 M6 M7 M8 M9 M10 M11 M12 M1 M2 M3 M4 M5 M6 M7 M8 M9 M10 M11 M12 M1 M2 M3 M4 M5 M6 M7 M8 M9 M10 M11 M12 M1 M2 M3 M4 M5 M6 M7 M8 M9 M10 M11 M12 YEAR 1 YEAR 2 YEAR 3 YEAR 4  Pilot system will be operational in June 2022 (M25)  Still enough time to complete the pilot experiments Legend Task/Subtask Activity as planned Postponed activity Delay of activity
  • 10. The project leading to this application has received funding from the European Union’s Horizon 2020 research and innovation programme under grant agreement No 869318 CS1 Contacts sandra.casas@eurecat.org andrea.naves@eurecat.org