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CS 6 Karmiel, Shafdan
Kick-off meeting: September, 7th 2020
I. Sabbah, K. Baransi-Karkaby, N. Massalha, G. Horn, A. Aharoni, H. Raanan
Kiperwas, D. Iossifidis, E. Bizani, C. Christophoridis, M. Touloupi
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
Symbiosis in Karmiel and Shafdan:
Karmiel Shafdan
Current situation
- Pre-treatment
- Primary clarfier
- Activated sludge
- Tertiary treatment via SAT
Municipal /
Agro-industrial
WW
Shafdan
WWTP
400 K m3/d
- Pre-treatment
- Primary clarifier
- Activated sludge
- Sand filtration
Municipal /
Agro-industrial
WW and (demo
scale AAT)
Karmiel
WWTP
30 K m3/d
Municipal / Agro-
industrial WWTP
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
ENERGY - Task 1.3.3
Biogas production from anaerobic pre-treatment of
municipal and/or industrial wastewater in Karmiel
Partners:
OBJECTIVE:
Reducing the high organic load peaks in
WWTP main stream, caused by mixing with olive
mill and slaughterhouse wastewater, using
iimmobilized high rate anaerobic system (AAT).
Karmiel
WWTP
30 K m3/d
Municipal /
Agro-industrial
WW
(120 m3/d)
OMW
(0.5-2 m3/d)
OMW tank /
pre-treatment
Mixing
tank
AAT
Biogas recovery:
(8-15) m3/d
Scenario 1Scenario 2
Packed
resin bedOMW
(0.5-2 m3/d)
OMW tank /
pre-treatment
Mixing
tank
AAT
Tests under different ratios
of discharge
Biogas recovery:
(8-15) m3/d
Municipal /
Agro-industrial
WW
(120 m3/d)
Recovery of
polyphenols task
1.4.5
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
ENERGY - Task 1.3.4
Combining anaerobic biofilm treatment with membrane
filtration and activated carbon in Shafdan
OBJECTIVE:
Testing the efficiency of AnMBR based on
AAT combined with Activated carbon for
higher biogas production (biofouling
reduction/optimal operation) from mixed
domestic and agro-industrial wastewater
Partners:
Shafdan
WWTP
400 K m3/d
Agro-industrial
WW
(winery/dairy/OMW)
Tank/Pre-
treatment
AAT AnMBR/AC
Biogas recovery:
(3-5) m3/d
Municipal /
Agro-industrial
WW
12-24 m3/d
Mixing
tank
The project leading to this application has received funding from the European
Union’s Horizon 2020 research and innovation programme under grant agreement
No 8693185
MATERIAL - Task 1.4.5
Recovery of high-value products from olive mill
wastewater in Karmiel
OBJECTIVES:
Recovery of polyphenols from olive mill wastewater
Content of study:
- Pre-trials in lab-scale
- Pilot plant system with an adsorption column
- Extraction with pressurised hot water
Partners:
Karmiel
WWTP
30 K m3/d
Packed
resin bedOMW
(0.5-2 m3/d)
OMW tank /
pre-treatment
Mixing
tank
AAT
Tests under different
ratios of discharge
Biogas recovery:
(8-15) m3/d
Municipal /
Agro-industrial
WW
(120 m3/d)
Subcritical / hot
water extraction
Polyphenols
Removal
60% PolyP
removal
Polyphenol
Recovery

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ULTIMATE project - Case Study 3 in Rosignano, IT
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ULTIMATE project - Case Study 6 in Karmiel/Shafdan, IL

  • 1. CS 6 Karmiel, Shafdan Kick-off meeting: September, 7th 2020 I. Sabbah, K. Baransi-Karkaby, N. Massalha, G. Horn, A. Aharoni, H. Raanan Kiperwas, D. Iossifidis, E. Bizani, C. Christophoridis, M. Touloupi
  • 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 Symbiosis in Karmiel and Shafdan: Karmiel Shafdan Current situation - Pre-treatment - Primary clarfier - Activated sludge - Tertiary treatment via SAT Municipal / Agro-industrial WW Shafdan WWTP 400 K m3/d - Pre-treatment - Primary clarifier - Activated sludge - Sand filtration Municipal / Agro-industrial WW and (demo scale AAT) Karmiel WWTP 30 K m3/d Municipal / Agro- industrial WWTP
  • 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 ENERGY - Task 1.3.3 Biogas production from anaerobic pre-treatment of municipal and/or industrial wastewater in Karmiel Partners: OBJECTIVE: Reducing the high organic load peaks in WWTP main stream, caused by mixing with olive mill and slaughterhouse wastewater, using iimmobilized high rate anaerobic system (AAT). Karmiel WWTP 30 K m3/d Municipal / Agro-industrial WW (120 m3/d) OMW (0.5-2 m3/d) OMW tank / pre-treatment Mixing tank AAT Biogas recovery: (8-15) m3/d Scenario 1Scenario 2 Packed resin bedOMW (0.5-2 m3/d) OMW tank / pre-treatment Mixing tank AAT Tests under different ratios of discharge Biogas recovery: (8-15) m3/d Municipal / Agro-industrial WW (120 m3/d) Recovery of polyphenols task 1.4.5
  • 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 ENERGY - Task 1.3.4 Combining anaerobic biofilm treatment with membrane filtration and activated carbon in Shafdan OBJECTIVE: Testing the efficiency of AnMBR based on AAT combined with Activated carbon for higher biogas production (biofouling reduction/optimal operation) from mixed domestic and agro-industrial wastewater Partners: Shafdan WWTP 400 K m3/d Agro-industrial WW (winery/dairy/OMW) Tank/Pre- treatment AAT AnMBR/AC Biogas recovery: (3-5) m3/d Municipal / Agro-industrial WW 12-24 m3/d Mixing tank
  • 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 8693185 MATERIAL - Task 1.4.5 Recovery of high-value products from olive mill wastewater in Karmiel OBJECTIVES: Recovery of polyphenols from olive mill wastewater Content of study: - Pre-trials in lab-scale - Pilot plant system with an adsorption column - Extraction with pressurised hot water Partners: Karmiel WWTP 30 K m3/d Packed resin bedOMW (0.5-2 m3/d) OMW tank / pre-treatment Mixing tank AAT Tests under different ratios of discharge Biogas recovery: (8-15) m3/d Municipal / Agro-industrial WW (120 m3/d) Subcritical / hot water extraction Polyphenols Removal 60% PolyP removal Polyphenol Recovery