The document describes two operational demo cases in Israel - Karmiel and Shafdan. In Karmiel, an advanced anaerobic treatment process is used to produce biogas from municipal and olive mill wastewater. The system is operational and achieving its targets. In Shafdan, a new system combines anaerobic biofilm treatment with membrane filtration and activated carbon to produce biogas from agro-industrial wastewater. Laboratory experiments show initial biogas production. The system is also now operational. A separate process in Karmiel aims to recover polyphenols from olive mill wastewater using resin adsorption columns. Laboratory experiments indicate over 40% recovery is possible.
D1.2-Demonstrator Case Study Karmiel/ShafdanDrKristineJung
The document summarizes the operational demo cases for CS6 Shafdan & Karmiel. It describes the baseline technologies and ultimate solutions being tested at the Karmiel and Shafdan WWTPs. For Karmiel, an advanced anaerobic treatment process is producing biogas from municipal and olive mill wastewater, and lab experiments are recovering polyphenols from olive mill wastewater. At Shafdan, an anaerobic biofilm reactor combined with membrane filtration and activated carbon is being constructed to produce biogas from agro-industrial wastewater. Both projects are progressing on schedule with pilot systems operational or nearing operation.
D1.2-Demonstrator Case Study Karmiel/ShafdanDrKristineJung
This document describes the operational demo cases for CS6 at the Karmiel and Shafdan wastewater treatment plants. It provides status updates on multiple subtasks involving advanced anaerobic treatment and biogas production, as well as recovery of high-value products from olive mill wastewater. The advanced anaerobic treatment systems at both sites are now operational, including an immobilized high-rate reactor at Karmiel and an anaerobic biofilm membrane bioreactor at Shafdan. Pilot-scale systems are also operational for polyphenol recovery from olive mill wastewater at Karmiel using adsorption and extraction. Laboratory experiments show promising results for biogas production and polyphenol removal.
D1.2-Demonstrator Case Study Karmiel/ShafdanDrKristineJung
This document describes two operational demo cases in Israel: Karmiel and Shafdan. In Karmiel, an advanced anaerobic treatment (AAT) system is processing municipal and olive mill wastewater to produce biogas. The AAT system has been constructed and is operational. In Shafdan, an anaerobic biofilm treatment membrane bioreactor (AnBTMBR) system combining AAT with activated carbon and membrane filtration has been constructed and started operation in August 2022, with sampling beginning in December 2022. The document provides details on the systems, including design, targets, status updates, operational procedures, and timeline updates for each location.
The document describes several operational demo cases for the CS7 Tain site. It summarizes the objectives, status, and timelines for multiple subtasks involving new technologies:
1) An RO system to treat distillery wastewater for internal water reuse, with a design capacity of 1 m3/d. The system is detailed designed and parts have been ordered.
2) A heat recovery system using heat exchangers to recover heat from treated distillery wastewater and reduce energy demands. The design is complete and parts have been ordered.
3) A two-stage system to recover nutrients from distillery wastewater involving struvite precipitation followed by ammonia stripping. The design is finished
The document summarizes a pilot project in Kalundborg, Denmark that is testing novel membrane treatment technologies to produce high-quality water for reuse from municipal wastewater effluent. Two pilot plants were constructed to test a conventional ultrafiltration membrane versus a novel tight ultrafiltration membrane, followed by reverse osmosis. The goals are to increase water reuse, reduce energy usage, and explore nutrient/product recovery. Water quality data and pilot performance will be evaluated under different treatment scenarios to assess water production and fouling prevention. Videos of the operating pilot plants are available online. The project is on schedule, with the pilots now operational.
The document describes the operational demo cases for CS7 Tain. It discusses several subtasks involving new technologies to treat and reuse distillery wastewater, including: 1) reverse osmosis to treat anaerobically digested wastewater for reuse, 2) heat recovery from treated wastewater, and 3) ammonia recovery via air stripping and struvite precipitation. Laboratory experiments and pilot demonstrations are underway or planned for various subtasks. The timelines indicate some delays but still sufficient time to complete the work by the end of the project.
The document discusses an operational demo case in Rosignano, Italy. It describes the current wastewater treatment situation and objectives to improve it using local by-products. Laboratory and pilot testing was conducted on activated hydrochar made from hydrochar, a waste product. Testing showed the hydrochar had higher COD and diclofenac removal rates than commercial activated carbon. By-products from local industries were also tested for softening, coagulation and flocculation, reducing COD and minerals. A pilot system was constructed using the hydrochar and is scheduled to be operational in June 2022 to further test and optimize the solutions. The timeline aims to have start-up results by month 19 and best practices identified by month 25
The document describes a pilot project in Nafplio, Greece to treat and reuse wastewater from a fruit processing plant. A mobile pilot plant was installed to extract high-value compounds from the wastewater using adsorption and subcritical water extraction. The residual wastewater would then be treated using an advanced oxidation process and a small bioreactor platform for polishing before being reused for irrigation or discharged. Laboratory experiments were conducted to test the individual technologies and the pilot units have been installed and are operational, with the goal of achieving 100% water reuse and a 90% reduction in freshwater use.
D1.2-Demonstrator Case Study Karmiel/ShafdanDrKristineJung
The document summarizes the operational demo cases for CS6 Shafdan & Karmiel. It describes the baseline technologies and ultimate solutions being tested at the Karmiel and Shafdan WWTPs. For Karmiel, an advanced anaerobic treatment process is producing biogas from municipal and olive mill wastewater, and lab experiments are recovering polyphenols from olive mill wastewater. At Shafdan, an anaerobic biofilm reactor combined with membrane filtration and activated carbon is being constructed to produce biogas from agro-industrial wastewater. Both projects are progressing on schedule with pilot systems operational or nearing operation.
D1.2-Demonstrator Case Study Karmiel/ShafdanDrKristineJung
This document describes the operational demo cases for CS6 at the Karmiel and Shafdan wastewater treatment plants. It provides status updates on multiple subtasks involving advanced anaerobic treatment and biogas production, as well as recovery of high-value products from olive mill wastewater. The advanced anaerobic treatment systems at both sites are now operational, including an immobilized high-rate reactor at Karmiel and an anaerobic biofilm membrane bioreactor at Shafdan. Pilot-scale systems are also operational for polyphenol recovery from olive mill wastewater at Karmiel using adsorption and extraction. Laboratory experiments show promising results for biogas production and polyphenol removal.
D1.2-Demonstrator Case Study Karmiel/ShafdanDrKristineJung
This document describes two operational demo cases in Israel: Karmiel and Shafdan. In Karmiel, an advanced anaerobic treatment (AAT) system is processing municipal and olive mill wastewater to produce biogas. The AAT system has been constructed and is operational. In Shafdan, an anaerobic biofilm treatment membrane bioreactor (AnBTMBR) system combining AAT with activated carbon and membrane filtration has been constructed and started operation in August 2022, with sampling beginning in December 2022. The document provides details on the systems, including design, targets, status updates, operational procedures, and timeline updates for each location.
The document describes several operational demo cases for the CS7 Tain site. It summarizes the objectives, status, and timelines for multiple subtasks involving new technologies:
1) An RO system to treat distillery wastewater for internal water reuse, with a design capacity of 1 m3/d. The system is detailed designed and parts have been ordered.
2) A heat recovery system using heat exchangers to recover heat from treated distillery wastewater and reduce energy demands. The design is complete and parts have been ordered.
3) A two-stage system to recover nutrients from distillery wastewater involving struvite precipitation followed by ammonia stripping. The design is finished
The document summarizes a pilot project in Kalundborg, Denmark that is testing novel membrane treatment technologies to produce high-quality water for reuse from municipal wastewater effluent. Two pilot plants were constructed to test a conventional ultrafiltration membrane versus a novel tight ultrafiltration membrane, followed by reverse osmosis. The goals are to increase water reuse, reduce energy usage, and explore nutrient/product recovery. Water quality data and pilot performance will be evaluated under different treatment scenarios to assess water production and fouling prevention. Videos of the operating pilot plants are available online. The project is on schedule, with the pilots now operational.
The document describes the operational demo cases for CS7 Tain. It discusses several subtasks involving new technologies to treat and reuse distillery wastewater, including: 1) reverse osmosis to treat anaerobically digested wastewater for reuse, 2) heat recovery from treated wastewater, and 3) ammonia recovery via air stripping and struvite precipitation. Laboratory experiments and pilot demonstrations are underway or planned for various subtasks. The timelines indicate some delays but still sufficient time to complete the work by the end of the project.
The document discusses an operational demo case in Rosignano, Italy. It describes the current wastewater treatment situation and objectives to improve it using local by-products. Laboratory and pilot testing was conducted on activated hydrochar made from hydrochar, a waste product. Testing showed the hydrochar had higher COD and diclofenac removal rates than commercial activated carbon. By-products from local industries were also tested for softening, coagulation and flocculation, reducing COD and minerals. A pilot system was constructed using the hydrochar and is scheduled to be operational in June 2022 to further test and optimize the solutions. The timeline aims to have start-up results by month 19 and best practices identified by month 25
The document describes a pilot project in Nafplio, Greece to treat and reuse wastewater from a fruit processing plant. A mobile pilot plant was installed to extract high-value compounds from the wastewater using adsorption and subcritical water extraction. The residual wastewater would then be treated using an advanced oxidation process and a small bioreactor platform for polishing before being reused for irrigation or discharged. Laboratory experiments were conducted to test the individual technologies and the pilot units have been installed and are operational, with the goal of achieving 100% water reuse and a 90% reduction in freshwater use.
The document provides details about operational demo cases for CS5 Lleida. It summarizes the status and progress of various subtasks involving new technologies to improve wastewater treatment and resource recovery at the Lleida brewery. These include a pilot system for water reuse using NF, RO and AOP/UV (subtask 1.2.5), an AnMBR and SOFC for energy production from wastewater (subtask 1.3.2), and plans for an ELSAR reactor. The NF, RO and SOFC systems are currently being installed and commissioned, while the ELSAR awaits building permits. Photos show the installed treatment systems and design drawings.
This document discusses the operational demo cases for the CS3 site in Rosignano, Italy. It summarizes the status of Subtask 1.4.2, which aims to use by-products from local industries for wastewater treatment. Laboratory and pilot tests show that activated hydrochar produced better adsorption results for COD and diclofenac removal compared to commercial activated carbon. Pilot systems for adsorption, advanced oxidation, and clariflocculation are being constructed and tested to further improve wastewater treatment using local by-products.
This document summarizes a pilot project testing novel membrane treatments for water reuse from municipal wastewater treatment plants in Kalundborg, Denmark. The project aims to produce high-quality water using ultrafiltration or nanofiltration followed by reverse osmosis to increase water recycling. Pilot plants are operating two treatment trains - one with a conventional ultrafiltration membrane and one with a novel ultra-tight ultrafiltration membrane. The pilots aim to compare membrane performance in preventing fouling and producing water suitable for reuse. Initial results indicate the task is progressing on schedule despite issues with pre-treatment options due to energy supply problems.
The document discusses two operational demo cases in Nafplio, Greece. The first case involves reusing wastewater from a fruit processing plant through a hybrid adsorption/SubCritical Water Extraction process to extract high-value compounds for reuse. The treated wastewater will then be further polished and reused for irrigation. The second case involves recovering antioxidants from the wastewater through adsorption and extraction processes. Laboratory experiments showed these processes can recover 50-70% of polyphenols. Pilot plants for both cases have been designed and are being constructed to test the technologies at a larger scale.
This document discusses a pilot project to increase reclaimed water availability for an industrial complex in Tarragona, Spain. The project involves testing new technologies at a wastewater treatment plant and future industrial wastewater treatment plant to polish wastewater and produce additional reclaimed water. Bench scale experiments were completed with various technologies like ultrafiltration, reverse osmosis, and membrane distillation. A pilot plant was ordered to test ultrafiltration, reverse osmosis, and zeolite adsorption. The pilot system is scheduled to be operational in September 2022 to evaluate increasing reclaimed water production by at least 20% with lower energy demand.
The document discusses a pilot project in Tarragona, Spain that aims to increase reclaimed water availability for a petrochemical complex by 20%. It involves upgrading an existing water resource recovery plant (WRRP) and future industrial wastewater treatment plant (iWWTP) using new technologies like ultrafiltration, reverse osmosis, membrane distillation, and zeolite adsorption. Bench and pilot tests of these technologies have been completed. The pilot plant is now operational and being monitored to test the technologies and achieve the goal of reducing fresh water usage.
Five techniques for reducing environmental impact in horticulture were showcased: (1) sodium removal from irrigation water using electrodialysis, (2) use of photocatalytic materials to reduce disease and break down plant protection products, (3) phosphorus removal using electrochemical precipitation, (4) particle removal from drain water using filtration without back washing, and (5) reducing nitrate content in soil using a KNS table for fertigation. A demonstration trial in 2017 of strawberry fertigation using a KNS table showed reduced nitrogen content in soil after harvest while maintaining crop growth, production and fruit quality.
This document discusses a case study in Tarragona, Spain to increase reclaimed water availability using new technologies. The current water resource plant and upcoming industrial wastewater treatment plant were described. The objectives are to increase reclaimed water production by 20% through membrane distillation, reverse osmosis, and ammonia removal via zeolite adsorption. Bench and pilot testing have been completed, with a pilot plant scheduled to operate starting in June 2022 to test ultrafiltration, reverse osmosis, and membrane distillation. The goal is to validate these new technologies and increase circular water usage at the petrochemical complex.
The document discusses an operational demo case in Rosignano, Italy. It describes the current wastewater treatment situation and objectives to improve it using local by-products. Pilot systems are being tested using adsorption columns with activated hydrochar and an AOP pilot plant. Initial results show reductions in COD and fluorescence indicators. The timeline outlines progress made so far and plans to complete pilot experiments and share best practices for material recovery.
D1.2-Demonstrator Case Study Saint-Maurice l´ExilDrKristineJung
The document discusses plans to develop pilot systems to recover sulfur from flue gas and wastewater treatment effluent at a chemical platform in Roussillon, France. A laboratory pilot plant is under construction to test sulfur recovery methods from flue gas involving condensation, dust cleaning, and scrubbing. Tests are also being prepared to recover sulfur from effluent using electrolytic oxidation, flocculation, or precipitation. An industrial pilot plant will then be built and connected to the site to further test sulfur recovery at scale. The overall goal is to develop sustainable solutions to recover 80% of sulfur from both streams and advance them to a technology readiness level of 6.
ULTIMATE project - Case Study 6 in Karmiel/Shafdan, ILDrKristineJung
addresses wastewater treatment, energy recovery via biogas production & the recovery of polyphenols within the #FoodIndustry, especially during wastewater shock loads
D1.2-Demonstrator Case Study Saint-Maurice l´ExilDrKristineJung
The document discusses plans to recover sulfur from flue gas and wastewater treatment plant effluent at a chemical platform in Roussillon, France. A laboratory pilot plant is under construction to test sulfur recovery techniques from flue gas using condensation, dust cleaning and scrubbing. Tests are also being prepared to recover sulfur from effluent using electrolytic oxidation, flocculation or precipitation. An industrial pilot plant will then be built to apply the optimal techniques identified from the laboratory testing to recover 80% of the sulfur from both sources. The status of the subtask is provided, including timelines showing the laboratory pilot becoming operational in June 2022 and plans for the industrial pilot in November 2022.
D1.2-Demonstrator Case Study Saint-Maurice l´ExilDrKristineJung
The document discusses plans to develop and test pilot systems for recovering sulfur and metals from waste streams at a chemical platform in Roussillon, France. A laboratory pilot for recovering sulfur from flue gases is already operational, and an industrial pilot plant is under construction. The industrial pilot will include two scrubbers to absorb remaining sulfur dioxide. Its components are being manufactured, with the goal of the system being operational by August 2023. Tests are also planned to recover sulfur from wastewater treatment plant effluent and to study the feasibility of recovering metals. The overall goal is to develop technologies to increase resource recovery and foster a circular economy at the chemical site.
The document discusses several operational demo cases for treating and recycling distillery wastewater in Tain, Scotland. It summarizes the status of various subtasks involving reverse osmosis (RO) treatment, heat recovery, and nutrient recovery through struvite precipitation and ammonia stripping. Laboratory and pilot experiments have been conducted on RO, stripping columns are in use, and initial results are promising for reducing water and energy usage through treatment and reuse.
This document summarizes the operational demo cases for CS4 Nafplio in Greece. Pilot wastewater treatment and recovery technologies are being implemented at a fruit processing plant to treat wastewater onsite for irrigation reuse. Laboratory experiments show the technologies effectively remove organic matter and recover high-value compounds. The pilot system has been installed and initial results are promising, with the goal of 100% water reuse for irrigation and reducing freshwater use by 90%.
This document discusses the status of various operational demo cases for the CS5 Lleida project. It summarizes the progress of Subtask 1.3.2, which involves anaerobic pretreatment of brewery wastewater and electricity production via solid-oxide fuel cell. The key technologies being tested are an anaerobic membrane bioreactor, an electrostimulated anaerobic reactor, and a solid oxide fuel cell. Pilot-scale tests indicate these technologies could produce biogas and electricity from wastewater at target capacities while advancing the technologies from TRL 7 to 9.
D1.2-Demonstrator Case Study Saint-Maurice l´ExilDrKristineJung
This document discusses a project to recover sulfur and metals from waste streams at a chemical platform in Roussillon, France. A laboratory pilot plant is currently operational to study sulfur dioxide absorption. An industrial pilot plant is under construction and aims to concentrate sulfur solutions and further absorb remaining SO2. The objectives are to recover 80% of sulfur from flue gases and wastewater treatment plant effluents. Tests on the laboratory pilot have begun and will continue, while the industrial pilot is scheduled to be operational by June 2023 to help advance circular economy goals at the chemical site.
D1.2-Demonstrator Case Study Nieuw PrinsenlandDrKristineJung
The document discusses two operational demo cases for the Ultimate project. For subtask 1.2.2, laboratory experiments are being conducted to optimize water reclamation from agricultural wastewater using electrodialysis. A pilot plant is being constructed and is expected to be operational by October 2022. For subtask 1.4.1, laboratory experiments aim to recover nutrients from wastewater through selective ion removal using electrodialysis. A pilot plant for nutrient recovery is also being constructed.
D1.2-Demonstrator Case Study Nieuw PrinsenlandDrKristineJung
The document discusses two operational demo cases for the Ultimate project. For subtask 1.2.2, laboratory experiments are optimizing water reclamation from agricultural wastewater using electrodialysis. Results show 60% reduction in salts. A pilot plant will be operational in September 2022 to test the solutions. For subtask 1.4.1, the same electrodialysis process is being used to recover nutrients like potassium, nitrogen, and calcium from wastewater. Laboratory experiments show over 55% recovery of various nutrients. Both pilot plants are on track to start operations and validate the technologies.
Using recycled concrete aggregates (RCA) for pavements is crucial to achieving sustainability. Implementing RCA for new pavement can minimize carbon footprint, conserve natural resources, reduce harmful emissions, and lower life cycle costs. Compared to natural aggregate (NA), RCA pavement has fewer comprehensive studies and sustainability assessments.
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The document provides details about operational demo cases for CS5 Lleida. It summarizes the status and progress of various subtasks involving new technologies to improve wastewater treatment and resource recovery at the Lleida brewery. These include a pilot system for water reuse using NF, RO and AOP/UV (subtask 1.2.5), an AnMBR and SOFC for energy production from wastewater (subtask 1.3.2), and plans for an ELSAR reactor. The NF, RO and SOFC systems are currently being installed and commissioned, while the ELSAR awaits building permits. Photos show the installed treatment systems and design drawings.
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The document discusses two operational demo cases in Nafplio, Greece. The first case involves reusing wastewater from a fruit processing plant through a hybrid adsorption/SubCritical Water Extraction process to extract high-value compounds for reuse. The treated wastewater will then be further polished and reused for irrigation. The second case involves recovering antioxidants from the wastewater through adsorption and extraction processes. Laboratory experiments showed these processes can recover 50-70% of polyphenols. Pilot plants for both cases have been designed and are being constructed to test the technologies at a larger scale.
This document discusses a pilot project to increase reclaimed water availability for an industrial complex in Tarragona, Spain. The project involves testing new technologies at a wastewater treatment plant and future industrial wastewater treatment plant to polish wastewater and produce additional reclaimed water. Bench scale experiments were completed with various technologies like ultrafiltration, reverse osmosis, and membrane distillation. A pilot plant was ordered to test ultrafiltration, reverse osmosis, and zeolite adsorption. The pilot system is scheduled to be operational in September 2022 to evaluate increasing reclaimed water production by at least 20% with lower energy demand.
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Five techniques for reducing environmental impact in horticulture were showcased: (1) sodium removal from irrigation water using electrodialysis, (2) use of photocatalytic materials to reduce disease and break down plant protection products, (3) phosphorus removal using electrochemical precipitation, (4) particle removal from drain water using filtration without back washing, and (5) reducing nitrate content in soil using a KNS table for fertigation. A demonstration trial in 2017 of strawberry fertigation using a KNS table showed reduced nitrogen content in soil after harvest while maintaining crop growth, production and fruit quality.
This document discusses a case study in Tarragona, Spain to increase reclaimed water availability using new technologies. The current water resource plant and upcoming industrial wastewater treatment plant were described. The objectives are to increase reclaimed water production by 20% through membrane distillation, reverse osmosis, and ammonia removal via zeolite adsorption. Bench and pilot testing have been completed, with a pilot plant scheduled to operate starting in June 2022 to test ultrafiltration, reverse osmosis, and membrane distillation. The goal is to validate these new technologies and increase circular water usage at the petrochemical complex.
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The document discusses plans to develop pilot systems to recover sulfur from flue gas and wastewater treatment effluent at a chemical platform in Roussillon, France. A laboratory pilot plant is under construction to test sulfur recovery methods from flue gas involving condensation, dust cleaning, and scrubbing. Tests are also being prepared to recover sulfur from effluent using electrolytic oxidation, flocculation, or precipitation. An industrial pilot plant will then be built and connected to the site to further test sulfur recovery at scale. The overall goal is to develop sustainable solutions to recover 80% of sulfur from both streams and advance them to a technology readiness level of 6.
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The growing significance of portable systems to limit power consumption in ultra-large-scale-integration chips of very high density, has recently led to rapid and inventive progresses in low-power design. The most effective technique is adiabatic logic circuit design in energy-efficient hardware. This paper presents two adiabatic approaches for the design of low power circuits, modified positive feedback adiabatic logic (modified PFAL) and the other is direct current diode based positive feedback adiabatic logic (DC-DB PFAL). Logic gates are the preliminary components in any digital circuit design. By improving the performance of basic gates, one can improvise the whole system performance. In this paper proposed circuit design of the low power architecture of OR/NOR, AND/NAND, and XOR/XNOR gates are presented using the said approaches and their results are analyzed for powerdissipation, delay, power-delay-product and rise time and compared with the other adiabatic techniques along with the conventional complementary metal oxide semiconductor (CMOS) designs reported in the literature. It has been found that the designs with DC-DB PFAL technique outperform with the percentage improvement of 65% for NOR gate and 7% for NAND gate and 34% for XNOR gate over the modified PFAL techniques at 10 MHz respectively.
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Introduction- e - waste – definition - sources of e-waste– hazardous substances in e-waste - effects of e-waste on environment and human health- need for e-waste management– e-waste handling rules - waste minimization techniques for managing e-waste – recycling of e-waste - disposal treatment methods of e- waste – mechanism of extraction of precious metal from leaching solution-global Scenario of E-waste – E-waste in India- case studies.
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
CS6: Karmiel and Shafdan
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
OMW +
municipal WW
Karmiel WWTP
municipal WW
Shafdan WWTP
- Activated sludge
- Tertiary treatment via SAT
- Pre-treatment
- Physical settling
- Activated sludge
- Sand filtration
AAT
Existing demo scale
CS6: Situation before Ultimate
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
Karmiel Shafdan
CS6: 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
CS6: Subtask 1.3.3 Status/progress - Karmiel
Subtask: 1.3.3 Biogas production from anaerobic pre-treatment of municipal and/or industrial wastewater in Karmiel
Baseline technology: Existing AAT demonstration plant
Ultimate solution to foster circular economy: Advanced Anaerobic Technology (AAT) for biogas production
Capacity: 120 m³/d
Quantifiable targets: 8-15 m³ biogas/d; 20-25% reduction of energy demand; 25% energy recovery
Status/progress:
• detailed design completed
• constructed and operational
TRL: 5 8
municipal WW: 98.4 – 99.6%;
olive mill WW: 0.4 – 1.6%
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
CS6: Current operational procedures and methodologies -
Karmiel
OMW… Olive mill wastewater
WWTP... Wastewater treatment plant
AAT ... Advanced anaerobic treatment
Subtask: 1.3.3 Biogas production from anaerobic pre-treatment of municipal and/or industrial wastewater in Karmiel
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
CS6: Picture of the high rate anaerobic reactor (AAT)
Subtask: 1.3.3 Biogas production from anaerobic pre-treatment of municipal and/or industrial wastewater in Karmiel
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
CS6: Task 1.3.3 is in time - Karmiel
✔
Subtask: 1.3.3 Biogas production from anaerobic pre-treatment of municipal and/or industrial wastewater in Karmiel
Immobilised anaerobic high rate reactor (AAT) is operational
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
CS6: Subtask 1.3.4 Status/progress - Shafdan
Subtask: 1.3.4 Combining anaerobic biofilm treatment with membrane filtration and activated carbon in Shafdan
Baseline technology: Biogas production via existing anaerobic digestion (AD)
Ultimate solution to foster circular economy: AAT with AC to prevent biomass inhibition
TRL: 5 7
Capacity: 12-24 m³/d
Quantifiable targets:
• 3-5 m³ biogas/d;
• 20-25% reduction of energy demand;
• 25% energy recovery
Status/progress:
• detailed design completed
• Constructed and operational
OMW… …….. Olive mill wastewater
WWTP............ Wastewater treatment plant
AnBTMBR ... Anaerobic biofilm treatment membrane bioreactor
10. 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
CS6: Results of the laboratory experiments
Subtask: 1.3.4 Combining anaerobic biofilm treatment with membrane filtration and activated carbon in Shafdan
The lab-scale: The start-up of the system has been. Below you can see
the picture of the lab-scale system with the first preliminary results of
rate of biogas production.
11. 11
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
CS6: Pictures of the anaerobic biofilm treatment
membrane bioreactor system
Subtask: 1.3.4 Combining anaerobic biofilm treatment with membrane filtration and activated carbon in Shafdan
12. 12
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
CS6: Pictures of the anaerobic biofilm treatment
membrane bioreactor system
Subtask: 1.3.4 Combining anaerobic biofilm treatment with membrane filtration and activated carbon in Shafdan
13. 13
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
CS6: Pictures of the anaerobic biofilm treatment
membrane bioreactor system
Subtask: 1.3.4 Combining anaerobic biofilm treatment with membrane filtration and activated carbon in Shafdan
14. 14
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
Subtask: 1.3.4 Combining anaerobic biofilm treatment with membrane filtration and activated carbon in Shafdan
CS6: Pictures of the anaerobic biofilm treatment
membrane bioreactor system
15. 15
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
CS6 Video: construction of the anaerobic biofilm treatment
membrane bioreactor system
Subtask: 1.3.4 Combining anaerobic biofilm treatment with membrane filtration and activated carbon in Shafdan
This video is accessible via
the indicated link below this
presentation on the
ULTIMATE webpage.
16. 16
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
Subtask: 1.3.4 Combining anaerobic biofilm treatment with membrane filtration and activated carbon in Shafdan
CS6: Pictures of the anaerobic biofilm treatment
membrane bioreactor system
17. 17
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
CS6: Operational procedures and methodologies Shafdan
Subtask: 1.3.4 Combining anaerobic biofilm treatment with membrane filtration and activated carbon in Shafdan
Agro-industrial
WW
(winery/dairy/OMW)
Storage tank AAT AC/AnMBR
Biogas recovery:
(3-5) m3/d
Municipal /
Agro-industrial
WW
12-24 m3/d
Mixing
tank
Shafdan
WWTP
Different rates:
0.2-2 m3/d
18. 18
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
CS6: Task 1.3.4 - Timeline - Shafdan
AnTBMBR is operational since August 2022
Still enough time to complete the experiments
Subtask: 1.3.4 Combining anaerobic biofilm treatment with membrane filtration and activated carbon in Shafdan
T1.3.4 - Combining anaerobic biofilm treatment with membrane
filtration and activated carbon in Shafdan
Baseline conditions assessed MS05 D1.1
Design of pilot system MS09
Laboratory scale experiments MS15
Pilot system operational MS15 +9M D1.2 + 3M
Start-up & results MS19 D1.9
Best practices for energy recovery D1.4
19. 19
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
CS6: Subtask 1.4.5 status/progress
Subtask: 1.4.5 Recovery of high-value products from olive mill wastewater in Karmiel
Baseline technology: No material recovery so far
Ultimate solution to foster circular economy:
Adsorption column with packed resin bed
and extraction with pressurized hot water
TRL: 5 7
Capacity: 0.2-2 m³/d
Quantifiable targets: > 40% Polyphenols recovery
Status/progress:
• Detailed design completed
• Lab scale experiments almost completed
0.2-2 m3/d
20. 20
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
Subtask: 1.4.5 Recovery of high-value products from olive mill wastewater in Karmiel
CS6: Pictures of the new technologies
Static adsorption
Lab scale – Dynamic adsorption
21. 21
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
Subtask: 1.4.5 Recovery of high-value products from olive mill wastewater in Karmiel
CS6: Operational procedures and
methodologies
22. 22
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
CS6: Results of the laboratory experiments
0.
3.5
7.
10.5
14.
0 15 30 45 60 75
adsorption
capacity
Q
(mg/g)
t (min)
0.1g
0.2g
0.5g
1.0g
y = -0,0195x + 2,9041
R² = 0,9964
y = -0,0208x + 2,6424
R² = 0,9802
y = -0,0197x + 2,3111
R² = 0,9701
0.
0.75
1.5
2.25
3.
3.75
0 15 30 45 60 75
lnQe
t (min)
0.1 g
0.2 g
0.5 g
Maximum adsorptive
capacity (Q): 23 g of
polyphenols per kg of
resin for the FPX 66 resin
Static
Adsorption
Dynamic
Adsorption
0
35
70
105
140
0. 125. 250. 375. 500.
C
phenols
(mg/L)
Bed Volums (BV)
2.5 ml/min
5ml/min
The breakthrough curves
showed that 1.7 m3 of
wastewater can be treated
per kg of resin per 10 cycles
Subtask: 1.4.5 Recovery of high-value products from olive mill wastewater in Karmiel
23. 23
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
CS6: Laboratory results
Subtask: 1.4.5 Recovery of high-value products from olive mill wastewater in Karmiel
•Static extraction experiments were
performed employing hot water and
organic solvents
•Water-methanol mixture (50:50 b.v.)
yielded 69% polyphenols recovery
•Currently working on dynamic extraction
experiments,
•Aiming to optimise:
• experimental conditions and
• solvent recovery and reuse strategy
24. 24
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
CS6: Task 1.4.5 – Timeline- Karmiel
Subtask: 1.4.5 Recovery of high-value products from olive mill wastewater in Karmiel
Pilot system expected to be operational in November 2022
Extension of lab-scale experiments to accelerate pilot start-up
and optimisation phases
Still enough time to complete the pilot experiments
25. 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
isabbah@gal-soc.org
CS6 Contacts
khalid@gal-soc.org